• Title/Summary/Keyword: Sludge Oil

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A Study on the Shape Optimization and Structural Analysis of the Suction Chamber for an ECO Vacuum Filter System (ECO Vacuum Filter System 용 흡입 챔버의 구조해석 및 형상 최적화에 관한 연구)

  • Lee, Choon-Man;Ha, Jae-Hyeon;Woo, Wan-Sik;Kim, Eun-Jung
    • Journal of the Korean Society for Precision Engineering
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    • v.33 no.12
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    • pp.971-977
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    • 2016
  • Recently, the problem of the accumulation of fine sludge from the cutting oil generated during machining processes has become a major threat to the environment. The fine sludge has adverse affects on the human body and the environment, and significantly contributes to marine pollution. However, a microfiltration technique that can process the sludge still needs to be studied and developed on a global scale. Therefore, it is necessary to develop eco-friendly equipment such as an ECO vacuum filter system and eco-friendly technologies for processing cutting oil. In this study, a structural analysis was carried out using a finite element method (FEM). Improved models of the suction chamber for the ECO vacuum filter system were proposed based on the analysis of the displacement and stress of the system. The model with the best result was then optimized using the commercial software, ANSYS. It was confirmed that, in the optimized model, displacement and stress were reduced in comparison with the initial model. Finally, the structural stability of the optimized model was verified through analysis.

Study on the Optimizing Ultrasonic Cell for Depth Measurement of Crude Oil (원유 깊이 측정을 위한 초전도셀 최적화에 관한 연구)

  • Oh, Kyutae
    • Journal of the Institute of Electronics and Information Engineers
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    • v.54 no.1
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    • pp.152-156
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    • 2017
  • Until now, most of the studies related to the ultrasonic sensor was in the water or the air. This study is for ultrasonic sensor in crude oil. because the ultrasonic cell use high voltage, it can cause an explosion. So, in crude oil, it did not use an ultrasonic sensor. This is the study of the ultrasonic sensor that generates ultrasonic waves while preventing explosion. Through this study, when trasmit ultrasonic in the crude oil, it found the most adaptive diameter, thickness, transmit frequency of ultrasonic cell to measure the depth of the crude oil and sludge. In conclusion, when a 200kHz frequency is generated by applying a voltage of 24V to the ultrasonic cell, the optimum diameter of ultrasonic cell is 26~28mm, the thickness of ultrasonic cell is 9mm.

Production of Biosurfactant by Pseudomonas aeruginosa EMS1 from Soybean Oil and Whey

  • Cha, Mi-Sun;Kim, Min-Joo;Lee, Kyung-Min;Son, Hong-Joo;Park, Eun-Hee;Lee, Sang-Joon
    • Environmental Sciences Bulletin of The Korean Environmental Sciences Society
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    • v.10 no.S_1
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    • pp.41-45
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    • 2001
  • Pseudomonas aeruginosa EMS1, isolated from activated sludge, was able to grow an produce a biosurfactant on 4.5 % soybean oil, used as the source of energy and carbon. Pseudomonas aeruginosa EMS1 was cultivated at 3$0^{\circ}C$ in a reciprocal shaking incubator, and the highest biosurfactant production was observed after 3 days. Furthermore, Pseudomonas aeruginosa EMS1 was also able to use whey as a co-substrate for biosurfactant production and growth

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Treatment of Oil Contaminated Groundwater Using DAF and Fenton Oxidation Process (DAF와 펜톤 산화 공정을 이용한 유류 오염 지하수 처리)

  • Lee, Chaeyoung
    • Journal of the Korean GEO-environmental Society
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    • v.11 no.10
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    • pp.49-55
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    • 2010
  • The oil spill occurred frequently due to probably the increased consumption of oil as the energy source and the raw materials of various chemicals. For the treatment of oil contaminated groundwater, DAF(Dissolved Air Flotation) is being used but the removal efficiency is low. Therefore it is necessary to reduce the free phase oil, oil-in water type or water-in oil type emulsified oil, and soluble oil which are the main sources of contaminated groundwater. In this study, treatment of contaminated groundwater was performed using the Fenton oxidation process. The optimum conditions for the removal of THP(Total Petroleum Hydrocarbon) were 3 of pH, 25mM of $H_2O_2$ concentration and 25mM of $Fe^{2+}$ concentration. THP and COD(Chemical Oxygen Demand) concentrations decreased less than 1.5mg/L and 40.0mg/L in 7 minutes using DAF and Fenton oxidation process. However it is necessary to install the settling basin as the sludge concentration increased approximately 5 times.

Introduction of KIER Pyrolysis Process and 3,000 ton/yr Demonstration Plant (KIER의 열분해유화 공정 기술과 실증플랜트 소개)

  • Shin, Dae-Hyun;Jeon, Sang-Gu;Kim, Kwang-Ho;Lee, Kyong-Hwan;Roh, Nam-Sun;Lee, Ki-Bong
    • 한국신재생에너지학회:학술대회논문집
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    • 2008.05a
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    • pp.479-482
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    • 2008
  • Since late of 2000, KIER has developed a novel pyrolysis process for production of fuel oils from polymer wastes. It could have been possible due to large-scale funding of the Resource Recycling R&D Center. The target was to develop an uncatalyzed, continuous and automatic process producing oils that can be used as a fuel for small-scale industrial boilers. The process development has proceeded in three stages bench-scale unit, pilot plant and demonstration plant. As a result, the demonstration plant having capacity of 3,000 tons/year has been constructed and is currently under test operation for optimization of operation conditions. The process consisted of four parts ; feeding system, cracking reactor, refining system and others. Raw materials were pretreated via shredding and classifying to remove minerals, water, etc. There were 3 kind of products, oils(80%), gas(15%), carbonic residue(5%). The main products i.e. oils were gasoline and diesel. The calorific value of gas has been found to be about 18,000kcal/$m^3$ which is similar to petroleum gas and shows that it could be used as a process fuel. Key technologies adopted in the process are 1) Recirculation of feed for rapid melting and enhancement of fluidity for automatic control of system, 2) Tubular reactor specially-designed for heavy heat flux and prevention of coking, 3)Recirculation of heavy fraction for prevention of wax formation, and 4) continuous removal & re-reaction of sludge for high yield of main product (oil) and minimization of residue. The advantages of the process are full automation, continuous operation, no requirement of catalyst, minimization of coking and sludge problems, maximizing the product(fuel oil) yield and purity, low initial investment and operation costs and environment- friendly process. In this presentation, background of pyrolysis technology development, the details of KIER pyrolysis process flow, key technologies and the performances of the process will be discussed in detail.

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Application of a Thermophilic Aerobic Digestion Process to Industrial Waste Activated Sludge Treatment

  • Kim, Young-Kee;Eom, Yong-Suk;Oh, Byung-Keun;Lee, Won-Hong;Choi, Jeong-Woo
    • Journal of Microbiology and Biotechnology
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    • v.11 no.4
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    • pp.570-576
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    • 2001
  • Thermophilic aerobic bacteria were applied in the degradation of industrial waste activated sludge (WAS) on a laboratory scale expreiment. The performance of digestion was estimated by measuring the reduction of total suspended solids (TSS), dissolved organic carbon (DOC), and total organic carbon (TOC). Among three strains of Bacillus stearothermophilus and three strains of Thermus species, B. stearothemophilus ATCC 31197 showed the best overall efficiency level for the degradation of industrial WAS, which was collected from a wastewater treatment plant in an oil refinery factory. Industrial WAS coul be successfully detraded in a batch digestion with ATCC 31197. The stability of the digestion process with ATCC 31197 was successfully verified by semi-continuous (fill-and-draw) digestion experiment. From the results of this study, it was shown that the thermophilic aerobic digestion process with ATCC 31197 could efficiently be applied to the degradation of industrial WAS.

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Effect of The Impeller Discharge Angle on the Performance of a Spurt Vacuum Pump

  • Lee, Ji-Gu;Kim, Youn-Jea
    • Applied Science and Convergence Technology
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    • v.26 no.1
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    • pp.1-5
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    • 2017
  • The spurt vacuum pump is widely used to transfer sludge and slurry, and to control flow rate in a variety of processing fields, such as the oil, chemical, and fiber industries. The efficiency of the pump depends on the design parameters of the impeller, such as the number of blades, and the blade angle. In this study, the effect of the configuration of the impeller discharge angle of a spurt vacuum pump, which influences total head, shaft power, and efficiency, was numerically investigated using the commercial code, ANSYS CFX ver. 16.1. In addition, the performance of the pump was evaluated on the basis of the correlations between the total head, pump efficiency, and pressure distribution.

Analysis of Combustion Air Flow in Incinerator (소각로의 연소 공기 유동 해석)

  • Lee, Dong-Hyuk
    • Design & Manufacturing
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    • v.16 no.2
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    • pp.26-32
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    • 2022
  • It is known that the fluidized bed incinerator, which is the subject of analysis, shows excellent performance in heat and mass transfer due to excellent mixing and contact performance between fluidized sand and fuel, and also shows relatively good combustion characteristics thanks to good mixing and long residence time for low-grade fuels. have. In this study, air flow analysis is performed to understand the characteristics of co-firing of sludge, waste oil and solid waste in the fluidized bed incinerator, flow characteristics of flue gas, and discharge characteristics of pollutants.The fluidized bed incinerator subject to analysis is a facility that incinerates factory waste and general household waste together with sludge, with a processing capacity of 32 tons/day. to be. In addition, the operation method was designed for continuous operation for 24 hours. As a result, it can be seen that the lower combustion air and the introduced secondary air are changed to a strong turbulence and swirl flow form and exit through the outlet while rotating inside the freeboard layer. The homogeneous one-way flow form before reaching the secondary air nozzle has very high diffusivity with the high-speed jet flow of the nozzle.

Synthesis of High-purity Silicon Carbide Powder using the Silicon Wafer Sludge (실리콘 기판 슬러지로부터 고순도 탄화규소 분말 합성)

  • Hanjung Kwon;Minhee Kim;Jihwan Yoon
    • Resources Recycling
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    • v.31 no.6
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    • pp.60-65
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    • 2022
  • This study presents the carburization process for recycling sludge, which was formed during silicon wafer machining. The sludge used in the carburization process is a mixture of silicon and silicon carbide (SiC) with iron as an impurity, which originates from the machine. Additionally, the sludge contains cutting oil, a fluid with high viscosity. Therefore, the sludge was dried before carburization to remove organic matter. The dried sludge was washed by acid cleaning to remove the iron impurity and subsequently carburized by heat treatment under vacuum to form the SiC powder. The ratio of silicon to SiC in the sludge was varied depending on the sources and thus carbon content was adjusted by the ratio. With increasing SiC content, the carbon content required for SiC formation increased. It was demonstrated that substoichiometric SiCx (x<1) was easily formed when the carbon content was insufficient. Therefore, excess carbon is required to obtain a pure SiC phase. Moreover, size reduction by high-energy milling had a beneficial effect on the suppression of SiCx, forming the pure SiC phase.

Environmental Impact Evaluation on Landfill Treatment of Petro-Chemical Wastewater Sludge by Life Cycle Assessment (전과정평가를 이용한 석유화학 폐수처리슬러지의 매립처리에 대한 환경영향평가)

  • Kim, Hyeong-Woo;Park, Hung-Suck
    • Journal of Korean Society of Environmental Engineers
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    • v.38 no.11
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    • pp.589-595
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    • 2016
  • This study evaluated the environmental impacts for landfill treatment of the wastewater treatment sludge (WTS) from petrochemical firms by life cycle assessment (LCA) and reviewed the impact reduction by landfill gas (LFG) utilization. The functional unit was 'landfill of 1 ton of WTS', and the system boundary included the process of input and treatment for WTS in landfill site. The impacts were high at landfill process (LP) and leachate treatment process (LTP). Global warming (GWP) and photochemical oxidants creation (POCP) were high at LP, while abiotic depletion (ADP), acidification (AP), eutrophication (EP), ozone depletion (ODP) were high at LTP. The major substances of various impact categories were crude oil (ADP), $NO_X$ (AP, EP), $CH_4$ (GWP, POCP), $Cl_2$ (ODP), respectively. The major factor of ADP, AP, EP was attributed from the generation of electricity used in LTP, and the methane within uncollected LFG was main factor of GWP and POCP. Therefore, electricity consumption reduction is identified to be an impact improvement option, and the flaring system installation or enhanced LFG recovery could be an alternative to reduce impacts. Among the various categories, GWP accounted the highest impact (${\geq}90%$) followed by ADP, POCP. In the avoidance impact resulted from the utilization of LFG, to substitute B-C oil or LNG showed the impact reduction of 32.7% and 12.0%, respectively.