• Journal of The Korean Society of Agricultural Engineers
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• v.51 no.2
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• pp.1-6
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• 2009

Acetogen과 같은 일부 혐기성미생물은 소위 acetyl-CoA 경로에 의해 아세트산, 에탄올, 그리고 몇 가지 생화학 물질을 생산한다. 이 경로에서는 일산화탄소를 기질로 이용할 수 있다. 일산화탄소 이외에 수소가 이용될 수 있다. 즉 이들 미생물은 독립영양생물로서 이산화탄소와 태양광에너지를 이용하는 녹색식물과 비유될 수 있으며, 일산화탄소는 탄소원으로서 동시에 에너지원으로서 이용된다. 본 연구에서는 혐기성 소화액 중 아세트산을 생성하는 미생물이 존재한다고 가정하고, 일산화탄소와 수소가 주 가연성분인 합성가스를 공급하면 추가의 메탄이 생성가능성을 평가하였다. 혐기성 소화과정에서 발생되는 메탄은 주로 아세트산으로부터 만들어지므로 일산화탄소를 공급하는 경우 추가로 메탄이 생성될 것으로 추측할 수 있기 때문이다. 이를 확인하기 위하여 현재 운영중인 바이오가스 생산 설비로부터 얻은 혐기성 소화액을 생물반응조에 넣은 후, 합성가스를 순환-공급하여 가스 생산량의 변화 및 조성을 분석하였다. 질소가스를 공급한 대조구와는 달리 일산화탄소 또는 합성가스를 공급한 경우에는 메탄가스가 생산되는 것을 확인하였다. 질소가스를 공급한 대조구와는 달리 일산화탄소 또는 합성가스를 공급한 경우에는 메탄가스가 생산되는 것을 확인하였다. 일산화탄소만을 공급했을 때에는 이산화탄소의 생성으로 가스 생산량이 증가하였으나, 수소가 포함된 합성가스를 공급하였을 때에는 이산화탄소가 탄소원이로 소비되어 가스 저장도 내의 가스량이 감소하는 것을 확인할 수 있었다. 가스화공정에 으해 얻어지는 합성가스는 온도와 가스 조성을 고러할 때, 바이오가스 생산을 위한 혐기성 소화조와 연계하면 소화조의 가온에 필요한 열을 공급할 수 있고 바이오가스 중 이산화탄소 농도를 낮추어 발열량을 개선할 수 있을 것으로 판단된다.

• Applied Chemistry for Engineering
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• v.23 no.6
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• pp.624-629
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• 2012

To capture and recover carbon dioxide ($CO_2$), we impregnated honeycomb made of ceramic paper with $K_2CO_3$ and its absorption characteristics of $CO_2$ were investigated. The absorption amount of $CO_2$ on the honeycomb absorbent impregnated with $K_2CO_3$ was 13.8 wt% at a constant temperature ($70^{\circ}C$) and relative humidity (66%) condition. Because the absorption amount of $CO_2$ achieved almost the same loading ratio of $K_2CO_3$ (17.6 wt%), the absorption reaction of $CO_2$ by $K_2CO_3$ on the honeycomb absorbent seems to be going smoothly. In addition, $CO_2$ absorption breakthrough characteristics of the honeycomb absorbent were analyzed at the temperature range of $50{\sim}80^{\circ}C$, and the water vapor was fed to an absorption column before the feeding of $CO_2$ or simultaneously with $CO_2$. As a result, the absorption capacity of $CO_2$ was more enhanced using the water vapor supplying before $CO_2$ than that of simultaneous supplying. It was confirmed by temperature programmed desorption analysis that the $KHCO_3$ produced by the absorption reaction of $K_2CO_3$ and $CO_2$ is regenerated by the desorption of $CO_2$ at a temperature of about $128^{\circ}C$.

• Applied Chemistry for Engineering
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• v.26 no.2
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• pp.205-209
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• 2015

CCU (Carbon Capture & Utilization) has a potential technology for the reduction and usage of carbon dioxide which is greenhouse gas emitting from a fossil fuel buring. To decompose the carbon dioxide, a three phase gliding arc plasma-catalytic reactor was designed and manufactured. Experiments of carbon dioxide reduction was performed by varying the gas flow rate with feeding the $CO_2$ only as well as the input power, the catalyst type and steam supply with respect to the injection of the mixture of $CO_2$ and $CH_4$. The $CO_2$ decomposition rate was 7.9% and the energy efficiency was $0.0013L/min{\cdot}W$ at a $CO_2$ flow rate of 12 L/min only. Carbon monoxide and oxygen was generated in accordance with the destruction of carbon dioxide. When the injection ratio of $CH_4/CO_2$ reached 1.29, the $CO_2$ destruction and $CH_4$ conversion rates were 37.8% and 56.6% respectively at a power supply of 0.76 kW. During the installation of $NiO/Al_2O_3$ catalyst bed, the $CO_2$ destruction and $CH_4$ conversion rates were 11.5% and 9.9% respectively. The steam supply parameter do not have any significant effects on the carbon dioxide decomposition.

• 한국신재생에너지학회:학술대회논문집
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• 2008.05a
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• pp.591-594
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• 2008

지구 온난화 문제의 심각성이 대두되면서 이산화탄소 저감 기술에 대한 관심이 증폭되고 있다. 가장 이상적인 방법은 탄소가 포함되지 않은 청정 재생 에너지원이지만, 에너지 공급 규모 면에서 보면 근미래에도 화석 연료가 에너지 수요에 대한 주요 공급원으로 남아있을 것이라는 의견이 지배적이다. 많은 화석 연료 중 천연가스는 탄소 배출량이 가장 적은 청정 연료로 지난 10년간 수요가 폭발적으로 증가해왔다. 이를 고려해볼 때 탄소 배출량이 적은 천연가스를 생산하면서 이산화탄소를 격리 시킬 수 있는 기술은 매우 매력적이다. 본 연구에서는 심해저의 메탄 하이드레이트로 부터 천연가스를 생산하는 기술로서 이산화탄소와 질소의 혼합 가스를 사용하는 기술 개발의 일환으로 혼합 가스에 의한 메탄 하이드레이트 해리 속도를 $^{13}C$ NMR을 이용해 측정한 결과를 제시하고자 한다.

• Korean Chemical Engineering Research
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• v.58 no.3
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• pp.396-407
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• 2020

As fossil fuels are depleted worldwide, alternative resources is required to replace fossil fuels, and biofuels are in the spotlight as alternative resources. Biofuels are produced from biomass, which is a renewable resource to produce biofuels or bio-chemicals. Especially, in order to substitute fossil fuels, the research focusing the biofuel (biodiesel) production based on CO₂ and biomass achieves more attention recently. To produce biomass-based biodiesel, the development of a supply chain network is required considering the amounts of feedstocks (ex, CO₂ and water) required producing biodiesel, potential locations and capacities of bio-refineries, and transportations of biodiesel produced at biorefineries to demand cities. Although many studies of the biomass-based biodiesel supply chain network are performed, there are few types of research handled the uncertainty in CO₂ supply which influences the optimal strategies of microalgae-based biodiesel production. Because CO₂, which is used in the production of microalgae-based biodiesel as one of important resources, is captured from the off-gases emitted in power plants, the uncertainty in CO₂ supply from power plants has big impacts on the optimal configuration of the biodiesel supply chain network. Therefore, in this study, to handle those issues, we develop the two-stage stochastic model to determine the optimal strategies of the biodiesel supply chain network considering the uncertainty in CO₂ supply. The goal of the proposed model is to minimize the expected total cost of the biodiesel supply chain network considering the uncertain CO₂ supply as well as satisfy diesel demands at each city. This model conducted a case study satisfying 10% diesel demand in the Republic of Korea. The overall cost of the stochastic model (US$ 12.9/gallon·y) is slightly higher (23%) than that of the deterministic model (US$ 10.5/gallon·y). Fluctuations in CO₂ supply (stochastic model) had a significant impact on the optimal strategies of the biodiesel supply network.

• Membrane Journal
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• v.16 no.3
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• pp.204-212
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• 2006

A numerical analysis was carried out for separation of carbon dioxide from carbon dioxide/nitrogen gas mixture by a polyethersulfone hollow fiber membrane which has shown a good stability against plasticization by carbon dioxide and an excellent separation efficiency fur carbon dioxide from its gas mixture. A computer program for carbon dioxide separation was developed using the Compaq Visual Fortran 6.6 software. Governing module equations were thought to be an initial-value problem and the nonlinear ordinary differential equations were simultaneously solved using the Runge-Kutta-Verner fifth-order method. From results of numerical analysis, the carbon dioxide partial pressure of the feed stream, the pressure ratio of the feed side to the permeate side and the feed gas residence time at the inside of a membrane were found to be very important factors to affect the permeation characteristics of carbon dioxide.

• Journal of Bio-Environment Control
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• v.18 no.1
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• pp.29-39
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• 2009

The influence of windbreak to minimize the ventilation velocity near the plant canopy of a greenhouse strawberry was thoroughly investigated using computational fluid dynamics (CFD) technology. Windbreaks were constructed surrounding the plant canopy to control ventilation and maintain the concentration of the supplied $CO_2$ from the soil surface close to the strawberry plants. The influence of no windbreak, 0.15 m and 0.30 m height windbreaks with varied air velocity of 0.5, 1.0 and 1.5 m/s were simulated in the study. The concentrations of supplied $CO_2$ within the plant canopy of were measured. To simplify the model, plants were not included in the final model. Considering 1.0m/s wind velocity which is the normal wind velocity of greenhouses, the concentrations of $CO_2$ were approximately 420, 580 and 653 ppm ($1{\times}10^{-9}kg/m^3$) for no windbreak, 0.15 and 0.30 m windbreak height, respectively. Considering that the maximum concentration of $CO_2$ for the strawberry plants was around 600-800 ppm, the 0.30 m windbreak height is highly recommended. This study revealed that the windbreak was very effective in preserving $CO_2$ gas within the plant canopy. More so, the study also proved that the CFD technique can be used to determine the concentration of $CO_2$ within the plant canopy for the plants consumption at any designed condition. For an in-depth application of this study, the plants as well as the different conditions for $CO_2$ utilization, etc. should be considered.

• Korean Chemical Engineering Research
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• v.55 no.3
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• pp.332-340
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• 2017

This study aims to propose a new optimization-based approach for design and analysis of the stand-alone hybrid energy supply system using renewable energy sources (RES). In the energy supply system, we include multiple energy production technologies such as Photovoltaics (PV), Wind turbine, and fossil-fuel-based AC generator along with different types of energy storage and conversion technologies such as battery and inverter. We then select six different regions of Korea to represent various characteristics of different RES potentials and demand profiles. We finally designed and analyzed the optimal RES stand-alone energy supply system in the selected regions using multiobjective optimization (MOOP) technique, which includes two objective functions: the minimum cost and the minimum $CO_2$ emission. In addition, we discussed the feasibility and expecting benefits of the systems by comparing to conventional systems of Korea. As a result, the region of the highest RES potential showed the possibility to remarkably reduce $CO_2$ emissions compared to the conventional system. Besides, the levelized cost of electricity (LCOE) of the RES-based energy system is identified to be slightly higher than conventional energy system: 0.35 and 0.46 $/kWh, respectively. However, the total life-cycle emission of $CO_2$ ($LCE_{CO2}$) can be reduced up to 470 g$CO_2$/kWh from 490 g$CO_2$/kWh of the conventional systems.

• Journal of the Korean GEO-environmental Society
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• v.24 no.6
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• pp.5-11
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• 2023

The engineering industry heavily relies on fossil fuels such as coal and petroleum to generate energy through combustion. However, this process emits carbon dioxide into the atmosphere, leading to global warming. To mitigate this issue, researchers have explored various methods to reduce carbon dioxide emissions, one of which is carbon dioxide underground storage technology. This innovative technology involves capturing carbon dioxide from industrial plants and injecting it into the saturated ground layer beneath the earth's surface, storing it securely underground. Despite its potential benefits, carbon dioxide underground storage efficiency needs improvement to optimize storage in a limited space. To address this challenge, our research team has focused on improving storage efficiency by utilizing surfactants. Furthermore, we evaluated how different carbon dioxide states, including gaseous, liquid, and supercritical, impact storage efficiency based on their respective pressures and temperatures within the underground reservoir. Our findings indicate that using surfactants and optimizing the injection rate can effectively enhance storage efficiency across all carbon dioxide states. This research will pave the way for more efficient carbon dioxide underground storage, contributing to mitigating the environmental impact of fossil fuels on the planet.

• 한국신재생에너지학회:학술대회논문집
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• 2007.11a
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• pp.433-436
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• 2007

가스화기술은 화석연료에 의한 기존의 화력발전기술을 대체할 수 있는 차세대 발전기술로 여겨지고 있어 전 세계적으로 기술개발은 물론 상용 플랜트를 앞 다투어 도입 건설 중에 있다. 현재 국내에서도 2014년까지 실증플랜트 완공에 매진을 가하고 있는 실정이다. 가스화기술은 온실가스인 이산화탄소를 동시에 감축하면서 전력뿐만 아니라 수소, DME, 화학원료와 같은 2차 고급 에너지원을 생산할 수 있다는 장점을 가지고 있다. 이 연구에서는 ASPEN plus를 이용하여 다양한 원료 공급에 따른 300 MW급 IGCC 플랜트에 대한 운전 특성을 알아보고자 하였다. 가스화기에 공급되는 원료는 석탄(역청탄), 중질유(납사, 벙커C유) 등으로 구분해 고려하였으며, 가스화 플랜트 해석모델에 대한 성능을 평가하기 위하여 해외에서 운전 중인 상용 IGCC 플랜트에 대한 운전자료와 상대오차로 비교 산출해 검증하였다. 그 다음으로 가스화(gasification)공정, 산가스 제거(acid gas removal)공정, 복합발전 공정(combined cycle)등과 같은 IGCC 플랜트를 구성하고 있는 각각의 단위공정에 대한 운전 특성에 대한 해석결과를 확인하였다. 해석 결과를 바탕으로 가스화기의 냉가스 효율(cold gas efficiency)과 탄소 전환율(carbon conversion), 산가스 제거공정에 대한 이산화탄소 포획 성능과 복합발전에 따른 플랜트 발전량 및 발전 효율(plant net efficiency)을 예측하였다.