• 자원ㆍ환경경제연구
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• 제21권2호
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• pp.417-439
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• 2012

최근 들어 고유가 상황이 지속되면서 정부는 연일 유가 안정 대책을 내놓고 있다. 특히 공정거래위원회는 혼합판매 허용을 골자로 하는 거래기준을 제시하였다. 본 연구는 혼합판매 도입과 활성화를 위한 정책적 방안을 제시하는 데 목적이 있다. 이를 위해 혼합판매와 관련된 국내 제도의 변천 과정을 기술한다. 또한 혼합판매 현황과 혼합판매 활성화를 위해 검토되어야 할 주요 사항들에 대해서도 논의한다. 혼합판매도입과 활성화를 위해서는 공급자별 구분저장 요건과 전량구매조건의 완화 내지 폐지가 선결될 필요가 있다. 이들 방안은 정유사 단계의 공급가격과 주유소 단계의 소비자가격 인하를 유도할 수 있는 긍정적인 효과를 발생시킬 수 있다. 또한 현행 법률 개정이 수반되어야 한다는 현실적인 제약을 고려할 때 중장기적으로 시장에서 대형마트 주유소, 독립형 자가폴, 프랜차이즈 독립폴 주유소를 육성하는 방안을 동시에 검토할 필요가 있다.

• 자원ㆍ환경경제연구
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• 제17권4호
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• pp.751-774
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• 2008

본 논문은 미국의 전력산업과 천연가스산업이 본격적인 구조변화를 시작한 1999년부터 2001년까지의 자료를 사용하여 제도적인 변화가 시장가격에 미친 영향을 분석한다. 이를 위해 가격에 영향을 미치는 비용과 수요를 제어한 축약형태(reduced forms) 모형의 회귀분석을 사용하여, 본 논문은 제도적인 요소 중에서 구체적으로 어떠한 요소가 가격결정과 긴밀히 연결되어 있는지를 추정한다. 분석결과에 의하면 투자자 소유의 기업의 전력가격이 공기업에 비해서 보다 높은 것으로 추정되었다. 더불어 전기와 천연가스 2개의 상품을 공급하는 기업은 1개의 재화를 제공하는 기업에 비해서 두 재화를 보다 저렴한 가격으로 공급하는 규모의 경제를 가지고 있는 것으로 나타났다. 마지막으로 천연가스 기업간의 합병은 합병이 일어나지 않은 지역에 비해서 가스요금의 수준이 보다 높은 것으로 나타났다.

• 한국가스학회지
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• 제7권4호
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• pp.30-35
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• 2003

제조물책임(Product Liability : PL)이란 제조물의 결함으로 인하여 소비자 또는 제3자의 생명, 신체, 재산 등에 손해가 발생했을 경우 그 제조물의 제조자 또는 판매자 등에게 손해배상 책임을 부과시키는 법으로 국내에서는 제조물책임법은 2002년 7월 시행되었다. 본 연구에서 FMEA를 이용한 화학제품의 제조물책임 대응체계를 구성하였으며, 깍N-Dimethyethylamine을 사례로 적용하여 연구를 진행하였다. 우선 화학제품의 취급설명서 역할을 하는 MSDS(Material Safety Data Sheet)를 통해 제품의 정보를 파악하고, 제품의 결함으로 인한 영향을 분석하는 FMEA기법을 적용하여 결함의 심각도, 결함의 발생빈도 및 검출도의 곱으로 정의된 RPN(Risk Priority Number)에 의하여 위험성을 정량적으로 제시하였다.

• 자원리싸이클링
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• 제8권5호
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• pp.34-43
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• 1999

폐윤활유로부터 활융가능한 연료기체를 생산하기 위해 개발한 전기아크를 이용한 분해자치에서 폐윤활유를 아크 분해할 때의 기체생성물과 잔류물의 특성을 연구하였다. 생성되는 기체는 수소(35~40%)와 아세틸렌(13~20%), 에틸렌(3~4%), 그 외 탄산수소들로 이루어져 있으며, 저온 열분해에서는 주요 생성물인 일산화탄소의 함량은 매우 적었다. 발생기체의 발열량은 11,000~13,000kacl/kg으로 기체 연료로의 활용성이 충분하여 유해기체도 배출기준치 이하였다. 액상 잔류물을 GC/MS로 분석한 결과 폐유의 고분자량 탄화수소물들이 저분자량 탄화수소물과 수소로 분해되었음을 알 수 있었고, 전지아크에 의한 고온 열분해이므로 탈수소반응이 주 반응임을 확인할 수 있었다. 고상 잔류물인 검댕이 평균 입경은 $10.3\mu\;extrm{m}$이며, 탄소 함량은 60%이상이고, 중금속 성분은 0.01ppm 이하였는데 전제과정을 거치 재활용이 가능할 것으로 생각된다.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2009년도 춘계학술대회 논문집
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• pp.451-454
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• 2009

Production and application of biodiesel are expected to grow steadily in the coming years and thus output of its by-product, crude glycerin, will accordingly increase as well. In the present study, gasification of biodiesel by-product as a renewable energy was performed in an entrained flow gasifier to investigate the gasification performance with the operating conditions. Crude glycerin shows a high heating value of 6,000 kcal/kg and low ash and sulphur content. Gasification was conducted in a temperature range of $950\;{\sim}\;1500\;^{\circ}C$. The variation of syngas composition with excess air ratio of 0.17 ~ 0.7 for air or oxygen as a gasification agent was investigated. From the results, syngas heating value, carbon conversion and cold gas efficiency of more than $2500\;kcal/Nm^3$, 95% and 65% were achieved, respectively. The temperature dependency of syngas composition, carbon conversion, and cold gas efficiency shows a similar tendency to excess air ratio at the temperature corresponding to the excess air ratio. The $H_2/CO$ ratio of the product gas was varied from 1.25 to 0.7 with the excess air ratio and this gas composition was favorable for DME synthesis. The optimum excess air ratio for gasification of biodiesel by-product was evaluated to be an approximately 0.35 to 0.4. The present results indicate that crude glycerin can be utilized as a feedstock for gasification to make syngas.

• 상하수도학회지
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• 제27권6호
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• pp.771-778
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• 2013

Gas hydrate (GH) process is a new desalination technology, where GH is a non- stoichiometric crystalline inclusion compounds formed by water and a number of gas molecules. Seawater GH is produced in a low temperature and a high pressure condition and they are separated from the concentrated seawater. The drawback of the GH process so far is that salt contents contained in its product does not meet the fresh water quality standard. This means that the GH process is not a standalone process for seawater desalination and it needs the help of other desalting process like reverse osmosis (RO). The objective of this study is to investigate the effect of GH process on energy saving for RO process in seawater desalination. The GH product water quality data, which were obtained from a literature, were used as input data for RO process simulation. The simulation results show that the energy saving effect by the GH process is in a range of 68 % to 81 %, which increases as the salt removal efficiency of the GH process increases. Boron (B) and total dissolved solids (TDS) concentrations of the final product of the hybrid process of GH and RO were also investigated through the RO process simulation to find relavant salt rejection efficiency of the GH process. In conclusion, the salt rejection efficiency of the GH process should exceed at least 78% in order to meet the product water quality standards and to increase the energy saving effect.

• Design & Manufacturing
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• 제12권1호
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• pp.18-25
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• 2018

Both injection and injection molding dies have evolved into advanced technology. Product quality is also evolving day after day. Therefore, the conditions of the injection mold and the injection conditions are becoming important. In order to improve the quality of the product, the Hardware part of the mold has developed as an advanced technology, and the Software part has also developed with advanced technology. This study deals with the cooling part, which is part of the hardware. In addition to fluid cooling, which is commonly used in the industry, by using gas cooling identify the phenomena that appear on the surface of the product and the critical point strain of the product to find the optimal cooling. Electronic parts and automobile parts whose surface condition is important, the cooling process is important to such a degree that they are divided with good products and defective products according to the cooling process at the time of injection. By controlling this important cooling and reducing the injection time with additional cooling, the product quality can be increased to the highest production efficiency. In addition, high efficiency can be achieved without additional investment costs. This study was conducted to apply these various advantages in the field.

• 환경위생공학
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• 제4권2호
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• pp.91-99
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• 1989

An anaerobic acidogenic fermentation experiment was carried out in order to investigate the distribution of volatile acid products and gas generations with varing temperatures and pH values. The experiment was carried out using $1\%$ glucose as substrate and a pair of 3.5 liter vessle as bench scale batch reactors. The reactors were operated for 7 days at 25, 30 and $35^{\circ}C$ and at pH values of 4.0, 4.5, 5.0, 5.5 and 6.0 at each temperature conditions. Major products at all experiment pH's at $35^{\circ}C$ were acetic acids and butyric acids which together composed around $90^{\circ}F$ of total product acids. At higher pH values at $35^{\circ}C$, propionic acid reached around $10\%$. At all experiment conditions, 52 to $55\%$ of generated gases comprised of hydrogen gas and 45 to $48\%$ of carbon dioxide. With temperature increase from 25 to $35^{\circ}C$, the production rate of acetic acid increased 2.9 fold, butyric acid 22 fold, hydrogen gas 2.0 fold and carbon dioxide gas 2.3 fold. Optimum reaction conditions for highest production of acetic acid and hydrogen gas was determined to be pH 5.5 at $35^{\circ}C$.

• Bulletin of the Korean Chemical Society
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• 제23권3호
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• pp.369-373
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• 2002

The liquid phase oxidation of p-xylene has been carried out with oxygen-enriched gas, and the manganese component was precipitated probably via over-oxidation to $Mn^{4+}$. The precipitation increased with rising oxygen concentration in the reaction gas and occurred mainly in the later part of the oxidation. The activity of the reaction decreased, and the blackening of the product and side reactions to carbon dioxide increased with the degree of precipitation. Precipitation can be decreased with the addition of metal ions, such as cerium, chromium and iron.

• 설비공학논문집
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• 제23권4호
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• pp.281-286
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• 2011

The objective of this study is to optimize the four-bed six-step pressure swing adsorption(PSA) process for high purity $CH_4$ recovery from the biogas. The effects of P/F(purge to feed) ratio and cycle time on the process performance were evaluated. The cyclic steady-states of PSA process were reached after 12 cycles. The purity and recovery rate of product gas, pressure and temperature changes were constant as the cycle repeated. It was shown that the P/F ratio gave significant effect on the product recovery rate by increasing the amount of purge gas in purge and regeneration step. The optimal P/F ratio was found to be 0.08. As the cycle time increased, the product purity decreased by increasing the feed gas flow rate. It was found that the optimal operating conditions were P/F ratio of 0.08 and total cycle time of 1,440 seconds with the purity of 97%.