• Title/Summary/Keyword: Carbon dioxide (CO2)

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A Study on Carbon Footprint and Mitigation for Low Carbon Apple Production using Life Cycle Assessment (전과정평가법을 이용한 사과의 탄소발생량 산정과 저감 연구)

  • Lee, Deog Bae;Jung, Sun Chul;So, Kyu Ho;Kim, Gun Yeob;Jeong, Hyun Cheol
    • Journal of Climate Change Research
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    • v.5 no.3
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    • pp.189-197
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    • 2014
  • Carbon footprint of apple was a sum of $CO_2$ emission in the step of manufacturing waste of agri-materials, and greenhouse gas emission during apple cultivation. Input amount of agri-materials was calculated on 2007 Income reference of Apple by Rural Development Administration. Emission factor of each agri- materials was based on domestic data and Ecoinvent data. $N_2O$ emission factor was based on 1996 IPCC guideline. Carbon dioxide was emitted 0.64 kg $CO_2$ to produce 1 kg apple fruit, and carbon dioxide was emitted 43.6% in the step of the manufacturing byproduct fertilizer, 1.3% in the step of the manufacturing single fertilizer, 4.7% in the step of the manufacturing composite fertilizer, 6.3% in the step of the manufacturing agri-chemicals, 14.6% in the step of the manufacturing fuel, 11.5% in the step of the fuel combustion, 17.7% of $N_2O$ emission by nitrogen application and 0.18% of disposal of agri-materials. It is needed for farmers to use fertilization recommendation based on soil testing (soil. rda.go.kr) because scientific fertilization is a major tools to reduce carbon dioxide of apple production. The fertilization recommendation could be also basic data in Measurable-ReporTablele-Verifiable (MRV) system for carbon footprint.

Effects of $Fe_{3}O_{4}$ Addition on Spinel Phase $LiMn_{2}O_{4}$ for $CO_{2}$ Decomposition (($CO_{2}$ 분해용 스피넬상 $LiMn_{2}O_{4}$에 대한 $Fe_{3}O_{4}$ 첨가효과)

  • Yang, Chun-Mo;Rim, Byung-O;Kim, Seung-Ho;Kim, Soon-Tae
    • Journal of the Korean Applied Science and Technology
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    • v.18 no.3
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    • pp.167-173
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    • 2001
  • The spinel $LiMn_{2}O_{4}$ powders were synthesized at $480^{\circ}C$ for 12 h in air by a sol-gel method using manganese acetate and lithium hydroxide as starting material and the $Fe_{3}O_{4}$ powders were synthesized by the precipitation method using $0.2M-FeSO_{4}{\cdot}H_{2}O$ and 0.5M-NaOH. The synthesized $Fe_{3}O_{4}$ powders were mixed at portion of 5, 10, 15 and 20 wt% about $LiMn_{2}O_{4}$ powders through ball-milling followed by drying at room temperature for 48 h in air. The mixed catalysts were reduced at $350^{\circ}C$ for 3 h by hydrogen and the decomposition rate of carbon dioxide was measured at $350^{\circ}C$ using the reduced catalysts. As the results of $CO_{2}$ decomposition experiments, the decomposition rates of carbon dioxide were 85% in all catalysts but the initial decomposition rates of $CO_{2}$ were slightly high in the case of the $5%-Fe_{3}O_{4}$ added catalyst.

Atmospheric Carbon Dioxide Levels in Garhwal Himalaya, India

  • Anthwal, Ashish;Joshi, V.;Joshi, S.C;Sharma, Archana;Kim, Ki-Hyun
    • Journal of the Korean earth science society
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    • v.30 no.5
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    • pp.588-597
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    • 2009
  • Measurements of atmospheric $CO_2$ were made in the mountainous region of Srinagar-Garhwal, India (January to December 2006). Concentrations of $CO_2$ averaged $393\pm4.9$ ppm in 2006. Daily variations of $CO_2$ values showed minimum during the daytime (376.2 ppm) and peaked in the morning/evening (410.1 ppm). At monthly intervals, the $CO_2$ values varied from $367\pm11.14$ (May) to $425.2\pm13.54$ ppm (March). If divided on a seasonal basis, the values declined to minimum amounts in post-monsoon ($389.9\pm9.0$ ppm) and reached maximums during winter ($397.1\pm11.6$ ppm). Although phenology is significant in controlling $CO_2$ levels, short-term changes cannot be explained without the anthropogenic perturbations (e.g., vehicular pollution and forest fires). The $CO_2$ concentrations in Srinagar-Garhwal (393.4 ppm) were generally higher than those of other major monitoring locations around the world.

Study on preparation of precipitated calcium carbonate using recycling water of ready-mixed Concrete (레미콘 회수수를 이용한 침강성 탄산칼슘 제조에 관한 연구)

  • Shin, Jae Ran;Kim, Jae Gang;Kim, Hae Gi;Kang, Ho Jong
    • Journal of the Korean Applied Science and Technology
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    • v.33 no.2
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    • pp.232-238
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    • 2016
  • In this study, a liquid carbonation method was applied for producing precipitate calcium carbonate by liquid-liquid reaction. Also a shuttle mechanism of wet chemical absorption using MEA was utilized. The high concentration $CO_2$(A) and exhaust gas(B) was used for collecting carbon dioxide in the 30% MEA aqueous solution, and $CO_2$ was fixed with rate of 0.35 mg of $CO_2$ per mg of sludge through the liquid carbonation process. It was found from SEM data that calcium carbonate was mainly made up with spherical vaerite with the mixing of a small quantity of calcite.

Supercritical $CO_2$ Extraction of Camptothecin and 10-hydroxycamptothecin from Camptotheca acuminata (초임계 $CO_2$를 이용한 Camptotheca acuminata에서 Camptothecin 및 10-hydroxycamptothecin 추출)

  • 부성준;변상요
    • KSBB Journal
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    • v.16 no.1
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    • pp.66-70
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    • 2001
  • Factors affecting the supercritical carbon dioxide extraction of camptothecin(CPT) and 10-hydroxycamptothecin(HCPT) from the dried powder of Cmptotheca acuminata were studied. Only a few amount of CPT and HCPT was extracted with pure supercritical carbon dioxide. Methanol and ethanol were efficient modifiers to extract CPT and HCPT. At $40^{\circ}C$, 250 bar, 1 mL/min flow rate, 41% of CPT and 35% of HCPT were extracted with supercritical carbon dioxide modified with 16% of methanol. The diffusion effect of HCPT on extraction efficiency was studied in this solid-fluid system. Round matrix hot-ball model assumption revealed that the value of D/$r^2$ was 0.0072 $min^{-1}$ which was higher than that of solvent extraction with methanol.

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Some Insights into the Basic QA/QC for the Greenhouse Gas Analysis: Methane and Carbon Dioxide (온실가스 기기분석의 정도관리를 위한 고려사항 연구 - CH4과 CO2를 중심으로 -)

  • Jeong, Jae-Hak;Lim, Ho-Soo;Kim, Ki-Hyun;Bae, Wi-Sup;Jeon, Eui-Chan
    • Journal of Korean Society for Atmospheric Environment
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    • v.22 no.5
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    • pp.712-718
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    • 2006
  • In order to investigate the analytical uncertainties associated with sampling and analysis of major greenhouse gaseous pollutants(carbon dioxide and methane), we attempted to quantify their adsorptive loss due to the contact with the container wall(such as Tedlar bag and vial). Using the GC/FID method, some basic experimental parameters(such as reproducibility and method detection limit) have been evaluated as part of the essential QA/QC The reproducibilities of carbon dioxide and methane were estimated as 2.02 and 0.2%, respectively. In addition, method detection limits were measured as 0.61 and 0.06 ng, respectively. A test of sample loss rate has also been made for Tedlar bag and vial by assessing the absolute amount of sample loss on the wall. By transferring the samples contained in Tedlar bag to various sizes of Tedlar bags, we measured differences in the absolute loss quantity due to such transfer. In addition, we also examined such loss mechanism as a function of elapsed time and light penetration rate for vial. As results, carbon dioxide and methane have shown about 2% of sample loss due to such contact. It is also noticed that the amount of loss with vial surface is lower than that of Tedlar bag. Therefore, field collection of greenhouse gases using various container types should be made more cautiously to minimize the possibility of sample loss and bias related to such loss.

Preparation of Honeycomb Carbon Dioxide Adsorbent Impregnated $K_2CO_3$ and Its Characterization ($K_2CO_3$를 담지시킨 고체 허니컴 이산화탄소 흡수제의 제조 및 이의 특성 평가)

  • Lee, Dong-Chul;Kim, Jin-Bae;You, Yoon-Jong
    • 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 $128^{\circ}C$.

Analysis of the Effect of Carbon Dioxide Reduction by Changing from Signalized Intersection to Roundabout using Tier 3 Method (Tier 3 방법을 이용한 회전교차로 도입에 따른 $CO_2$ 감축효과)

  • Lee, Jung-Beom;Lee, Seung-Hoon
    • The Journal of The Korea Institute of Intelligent Transport Systems
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    • v.10 no.5
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    • pp.105-112
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    • 2011
  • Delay reduction of vehicles at the intersection is highly dependent on the signal operation method. Improper traffic operation causes the violation of the traffic regulations and increasing traffic congestion. Delay because of congestion has contributed to the increase in carbon dioxide in the atmosphere. The focus of this paper is to measure the amount of carbon dioxide when the intersection is changed to roundabout. Even though, Intergovernmental Panel on Climate Change(IPCC) recommends Tier 1 method to measure the amount of greenhouse gas from vehicles, this paper used Tier 3 method because we could use the data of average running distance per each vehicle model. Two signalized intersections were selected as the study area and the delay reductions of roundabout operation were estimated by VISSIM microscopic simulation tool. The control delay for boksu intersection reduced from 28.6 seconds to 4.4 seconds and the KRIBB intersection sharply reduced from 156.4 seconds to 23.6 seconds. In addition, carbon dioxide for two intersections reduced to 646.5 ton/year if the intersection is changed to roundabout. Future research tasks include testing the experiment for networks, as well as for various intersection types.

Removal CO2 Using Na2CO3, K2CO3 and Li2CO3 Impregnated Activated Carbon -Characteristics of CO2 Adsorption in Fixed Bed Reactor- (Na2CO3, K2CO3 및 Li2CO3 첨착활성탄을 이용한CO2 제거 -고정층 반응기에서의 CO2 흡착특성-)

  • Choi, Won-Joon;Jung, Jong-Hyeon
    • Journal of Environmental Health Sciences
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    • v.34 no.3
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    • pp.240-246
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    • 2008
  • The purpose of this study was to gain basic information on the characteristics of $CO_2$ adsorption in relation to $Na_2CO_3$, $K_2CO_3$, $Li_2CO_3$-impregnated activated carbon in a Fixed Bed Reactor. From the results of this study the following conclusions were made: $Na_2CO_3$, $K_2CO_3$, $Li_2CO_3$-impregnated activated carbon had a longer breakthrough time and more enhanced adsorption capacity than activated carbon alone. When tested with isothermal adsorption and tested for $CO_2$ adsorption the amount of $CO_2$ adsorbed varied with temperature, $CO_2$ inlet concentration, gas flow rate, aspect ratio, etc. Based on the results, when Langmuir, Freundlich and Dubinin-Polanyi adsorption isotherms were used for linear regression of isothermal adsorption data, Langmuir adsorption isotherm was the most suitable. And, the optimum condition for $Na_2CO_3$ and $K_2CO_3$ impregnated activated carbon make-up was 1N and $Li_2CO_3$ was 0.1N. It could be concluded that adsorption capacity was decreased with adsorption temperature and increased gas concentration. When the aspect ratio (L/D) was varied 0.5, 1.0 and 2.0, the significant drop of adsorption amount was observed below 1.0 and breakthrough time was shortened with gas flow rate.