• 에너지공학
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• 제25권4호
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• pp.37-52
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• 2016

석유제품은 한국 및 일본 모두에서 1차 에너지원 중 소비 비중이 가장 높다. 이에 본 논문에서는 산업연관분석을 이용하여 한국 및 일본 정유산업의 국민경제적 역할을 비교 분석해 보고자 한다. 먼저 수요유도형 모형을 이용하여 정유산업의 생산유발효과 및 부가가치 유발효과를 살펴본다. 다음으로 공급유도형 모형 및 레온티에프 가격모형을 적용하여 각각 정유산업의 공급지장효과 및 물가파급효과를 분석한다. 이 과정에서 정유산업을 내생부문이 아닌 외생부문으로 다룸으로써 정유산업을 중심으로 한 논의결과를 제시한다. 수요유도형 모형의 분석 결과, 정유산업에서의 1원 생산이 타 산업에 미치는 생산유발효과는 한국 0.2620원 및 일본 0.6537원으로 일본의 값이 더 크다. 하지만 타 산업 부가가치 유발효과를 분석한 결과 각각 0.0946원 및 0.0536원으로 한국의 값이 일본의 값보다 크다. 정유산업 산출물 1원 어치의 공급지장이 타 산업에 미치는 부정적 생산차질효과를 의미하는 공급지장효과를 살펴보면, 한국 0.9657원 및 일본 1.4476원으로 일본 정유산업의 공급지장효과가 더 큰 것으로 분석되었다. 정유산업의 산출물 가격 10% 인상으로 인한 물가파급효과는 한국 0.3819% 및 일본 0.3409%로 한국의 값이 더 큰 것으로 분석되었다.

• 대한화학회지
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• 제58권1호
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• pp.76-79
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• 2014

Petroleum refinery effluents are waste originating from industries primarily engaged in refining crude oil. It is a very complex compound of various oily wastes, water, heavy metals and so on. Conventional processes are unable to effectively remove the chemical oxygen demand (COD) of petroleum refinery effluents. Supercritical water oxidation (SCWO) was proposed to treat petroleum refinery effluents. In this paper, methanol was used to investigate co-oxidative effect of methanol on petroleum refinery effluents treatment. The results indicated that supercritical water oxidation is an effective process for petroleum refinery effluents treatment. Adding methanol caused an increase in COD removal. When reaction temperature is $440^{\circ}C$, residence time is 20 min, OE is 0.5 and initial COD is 40000 mg/L, and COD removal increases 8.5%.

• 한국대기환경학회지
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• 제24권2호
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• pp.229-237
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• 2008

Hazardous air pollutants emitted from the oil refinery plant were surveyed from 1993 US and 2005 Korean TRI data. Toluene, xylene, methanol, MTBE and n-hexane, relatively large in amount of fugitive emission, are considered as candidates of newly designated HAPs in Korea. The sealed oil pump, one of equipments among fugitive sources in the crude oil distillation tower was examined for the estimation of amounts of annual HAPs emissions according to several calculation methods using registered emission factors. Emission rates showed to be decreased with following calculation factors; average emission factor>pegged emission factor>concentration emission factor>correlation equation. Annual emission amounts of benzene, toluene, xylene. ethyl benzene and nhexane from the distillation tower were estimated and amounts of these HAPs calculated with TVOC concentrations obtained from LDAR program and correlation equations showed only 6% of those from using concentration factors.

• Environmental Engineering Research
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• 제24권4호
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• pp.711-717
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• 2019

The application of advanced oxidation for the treatment of oil refinery wastewater under UV radiation by using nanoparticles of titanium dioxide was investigated. Synthetic wastewater prepared from phenol crystals; Power Glide SAE40 motor vehicle oil and water was used. Response surface methodology (RSM) based on the Box-Behnken design was employed to design the experimental runs, optimize and study the interaction effects of the operating parameters including catalyst concentration, run time and airflow rate to maximize the degradation of oil (SOG) and phenol. The analysis of variance and the response models developed were used to evaluate the data obtained at a 95% confidence level. The use of the RSM demonstrated the graphical relationship that exists between individual factors and their interactive effects on the response, as compared to the one factor at time approach. The obtained optimum conditions of photocatalytic degradation are the catalyst concentration of 2 g/L, the run time of 30 min and the airflow rate of 1.04 L/min. Under the optimum conditions, a 68% desirability performance was obtained, representing 81% and 66% of SOG and phenol degradability, respectively. Thus, the hydrocarbon oils were readily degradable, while the phenols were more resistant to photocatalytic degradation.

• 한국환경과학회지
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• 제13권7호
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• pp.703-710
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• 2004

Petroleum refineries have been considered as an important emission source for atmospheric volatile hazardous air pollutants(HAPs). The emission source includes petroleum refinery processes and process equipment. The control strategy for volatile HAPs requires emission estimations of these pollutants. However, systematic methods of volatile HAPs emission from petroleum refineries have not yet been established. Accordingly, present study surveyed the estimation method of volatile HAPs emitted from the petroleum refinery processes and process equipment. The emission estimation methods for the petroleum refinery processes are applied for 11 petroleum refining facilities: fluidized catalytic cracking, thermal cracking, moving bed catalytic cracking, compressed engine, blowdown system, vacuum distilled column condensator, natural gas or distilled boiler, natural gas or distilled heater, oil boiler, oil heater and flare. Four emission estimation methods applied for the petroleum refinery process equipment are as follows: average emission factor approach, screening ranges approach, EPA correlation approach and unit-specific correlation approach. The process equipment for which emission factors are available are valves, pump seals, connectors, flanges and open-ended lines.

• 한국연소학회:학술대회논문집
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• 한국연소학회 2014년도 제49회 KOSCO SYMPOSIUM 초록집
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• pp.255-257
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• 2014

The installation of light oil facilities or delayed cokers seems to be inevitable in the oil refinery industry due to the heavy crude oil reserves and the increased use of light fuels as petroleum products. Petroleum coke is a byproduct of oil refineries and it has higher fixed carbon content, higher calorific value, and lower ash content than coal. However, its sulfur content and heavy metal content are higher than coal. In spite of disadvantages, petroleum coke might be one of promising resources due to gasification processes. The gasification of petroleum coke can improve economic value of oil refinery industries by handling cheap, toxic wastes in an environment-friendly way. In this study, $CO_2$ gasification reaction kinetics of petroleum coke, various coals and mixing coal with petroleum coke have investigated and been compared by using TGA. The kinetics of $CO_2$ gasification has been performed with petroleum coke, 3 kinds of bituminous coal [BENGALLA, White Haven, TALDINSKY], and 3 kinds of sub-bituminous coal [KPU, LG, MSJ] at various temperature[$1100-1400^{\circ}C$].

• 한국항해항만학회:학술대회논문집
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• 한국항해항만학회 2002년도 춘계학술대회논문집
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• pp.73-87
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• 2002

• 한국마린엔지니어링학회:학술대회논문집
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• 한국마린엔지니어링학회 2006년도 전기학술대회논문집
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• pp.145-146
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• 2006

The main objective of this research is to develop a system which will provide a more efficient fuel saying measure for the current marine products industry situation caused by the increased cost of oil. For that function, the developed system has been verified using the medium of blending oil known as the MF 30 class. As a result, MF 30 was confirmed meeting the International Standard for NOx emissions and content of Sulfur. Oil composition and soot level analysis showed that it is acceptable to use MF 30 class in condition of proper engine running operation and pre-refinery treatment.

• 한국수산과학회지
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• 제8권2호
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• pp.73-84
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• 1975

1) 호남정유공장 폐수 및 부근에 버려진 유류와 사포리의 원유저장 탱크에서 흘러나온 유류는 썰물을 따라 여수해만 쪽으로 흘렸다가 밀물을 따라 백합양식장으로 바로 흘러 들어가며 대조일의 조수에서 $6\~8 $시간만에 양식장 전역에 이른다. 2) 지점 9, 10은 강수의 혼입이 약간 많은 수질인 즉 pH가 상대적으로 낮고 암모니아 질소가 많고 n-헥산 가용물질량이 적은 편이지만 지점 $6\~10$은 수질이 동일하다. 3) 폐수배출관이 있는 지점 2에서의 수질은 표층, 중층, 하층에 별다른 차가 없다. 4) 호남정유공장 폐수에 있어서 유해성분으로서 pH, 황화물이 배출기준 보다 높고, COD, 페놀, n-확산 가용물질량은 배출 기준보다 낮은 편이나 n-헥산가용물질량은 상당히 높은 수준이라고 본다. 5) 호남정유공장 폐수에 함유되어 있는 유해성분의 각 수역에서의 농도는 n-확산가용성 이외는 정상해수와 별로 다른 바 없다. 그러나 n-확산가용물질의 농도는 정상해수보다 높다. 6)해역에서의 n-헥산가용물질량 및 COD 값이 Table 1에서 볼 때 공장에 가까운 수역일수록 높은 것으로 보아 백합양식장에서의 이들 성분농도가 높은 원인은 해구유동도 참작할 때 호남정유공장의 폐수 및 누출유에 있다고 본다.

• 분석과학
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• 제16권5호
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• pp.399-406
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• 2003

본 연구는 수소화물 발생장치가 부착된 원자흡광 광도계 (HG-AAS)를 이용하여 비교적 고농도의 Se을 함유하고 있는 석유정제 폐수의 Se 분석을 위하여 적합한 분석조건을 선정하고자 수행되었다. Se(VI)의 Se(IV)로의 환원 실험에서 폐수량 10 mL, 염산 주입량 10 mL, 가열시간 30분이 최적 환원조건으로 결정되었다. 폐수의 조성성분과 유기물의 농도가 높은 경우에는 Se 회수율이 감소하였다. 따라서 3가지 산분해법 ($HNO_3/HClO_4$ 분해, $KMnO_4$ 분해 및 초단파 산분해)에 의한 유기물, 석유화합물 분해 및 유기성 Se(org.), Se(IV) 산화에 따른 Se 회수율을 검토하였다. 실험결과 산분해전 약 50~80%이었던 Se 회수율은 모든 산분해에서 90%이상이었으며 특히, 초단파 산분해에 의한 Se 회수율이 가장 높은 것으로 나타났다. 그러므로 HG-AAS를 이용한 석유정제 폐수의 Se 분석시에는 초단파 산분해후 염산 처리를 하는 전처리 과정이 가장 적합한 것으로 나타났다.