• Title/Summary/Keyword: process water

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A Study on Contact Arc Metal Cutting for Dismantling of Reactor Pressure Vessel (원자로 해체를 위한 수중 아크 금속 절단기술에 대한 연구)

  • Kim, Chan Kyu;Moon, Do Yeong;Moon, Il Woo;Cho, Young Tae
    • Journal of the Korean Society of Manufacturing Process Engineers
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    • v.21 no.1
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    • pp.22-27
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    • 2022
  • In accordance with the growing trend of decommissioning nuclear facilities, research on the cutting process is actively proceeding worldwide. In general, a thermal cutting process, such as plasma cutting is applied to decommissioning a nuclear reactor pressure vessel (RPV). Plasma cutting has the advantage of removing the radioactive materials and being able to cut thick materials. However, when operating under water, the molten metal remains in the cut plane and re-solidifies. Hence, cutting is not entirely accomplished. For these environmental reasons, it is difficult to cut thick metal. The contact arc metal cutting (CAMC) process can be used to cut thick metal under water. CAMC is a process that cuts metal using a plate-shaped electrode based on a high-current arc plasma heat source. During the cutting process, high-pressure water is sprayed from the electrode to remove the molten metal, known as rinsing. As the CAMC is conducted without using a shielding gas, such as Argon, the electrode is consumed during the process. In this study, CAMC is introduced as a method for dismantling nuclear vessels and the relationship between the metal removal and electrode consumption is investigated according to the cutting conditions.

Improvement of Organic Substances Indicators by Linked Ultra Violet-Advanced Oxidation Process After Ozonation for Anaerobic Digested Wastewater (소화탈리액 대상 오존 전처리와 Ultra Violet-Advanced Oxidation Process 연계 처리를 통한 유기물질 지표 개선)

  • Jaiyeop Lee;Jesmin Akter;Ilho Kim
    • Journal of Korean Society of Water and Wastewater
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    • v.37 no.5
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    • pp.253-259
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    • 2023
  • Bioreactors are devices used by sewage treatment plants to process sewage and which produce active sludge, and sediments separated by solid-liquid are treated in anaerobic digestion tanks. In anaerobic digestion tanks, the volume of active sludge deposits is reduced and biogas is produced. After dehydrating the digestive sludge generated after anaerobic digestion, anaerobic digested wastewater, which features a high concentration of organic matters, is generated. In this study, the decomposition of organic carbon and nitrogen was studied by advanced oxidation process. Ozone-microbubble flotation process was used for oxidation pretreatment. During ozonation, the TOC decreased by 11.6%. After ozone treatment, the TOC decreased and the removal rate reached 80.4% as a result of the Ultra Violet-Advanced Oxidation Process (UV-AOP). The results with regard to organic substances before and after treatment differed depending on the organic carbon index, such as CODMn, CODCr, and TOC. Those indexes did not change significantly in ozone treatment, but decreased significantly after the UV-AOP process as the linkage treatment, and were removed by up to 39.1%, 15.2%, and 80.4%, respectively. It was confirmed that biodegradability was improved according to the ratio of CODMn to TOC. As for the nitrogen component, the ammonia nitrogen component showed a level of 3.2×102 mg/L or more, and the content was maintained at 80% even after treatment. Since most of the contaminants are removed from the treated water and its transparency is high, this water can be utilized as a resource that contains high concentrations of nitrogen.

Development of a New Advanced Water Treatment Process (PMR) and Assessment of Its Treatment Efficiency (고도정수처리 신(新) 공정(PMR)개발 및 처리효율 평가)

  • Ahn, Hyo-Won;Noh, Soo-Hong;Kwon, Oh-Sung;Park, Yong-Hyo;Wang, Chang-Keun
    • Membrane Journal
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    • v.18 no.2
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    • pp.157-167
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    • 2008
  • Removal of organic substances and taste/odor control are ones of the main issues in water supply, resulting in introduction of advanced processes such as ozon/GAC, or PAC. However, raw water quality deteriorates, new pollutants advent, so water quality is not acceptable enough even with those existing advanced processes. In this paper, a new advanced water treatment process using PAC slurry blanket, where PAC particles stay in the basin as slurry blanket, coupled with submerged membranes is introduced. A pilot plant $(80m^3/day)$ was installed to assess the performance of this new process using actual raw water, and DOC was removed higher than 90% in the beginning and $70{\sim}80%$ afterwards, while 2-MIB and geosmin were removed completely. This new process still requires future study on process optimization and long-term assessment, however it seems highly possible to countermeasure as a new advanced process with high removal efficiency.

A study on boron removal for seawater desalination using the combination process of mineral cluster and RO membrane system

  • Cho, Bong-Yeon;Kim, Hye-Won;Shin, Yee-Sook
    • Environmental Engineering Research
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    • v.20 no.3
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    • pp.285-289
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    • 2015
  • Complicated and expensive seawater desalination technology is a big challenge in boron removal process. Conventional seawater desalination process of coagulation utilized for pre-treatment is difficult to remove boron. Boron can be removed more effectively in Reverse Osmosis (RO) process than any other processes. In this study, a coagulant with the name Mineral Cluster was examined its boron removal ability. Boron removal efficiency of Mineral Cluster depended on pH value and Mineral Cluster dosage. Desalination process combines the pre-treatment process with Mineral cluster diluted at the ratio of 1:2500 and the RO membrane process. The original sea water could be desalinated to drinking water quality, 1 mg/L, without any pH adjustments. Therefore, if the Mineral cluster is added without any other chemicals for adjusting pH, the desalination process would be much safer, efficient and economical.

[ $P_{\lambda,;,T}^M-policy$ ] of a finite dam with both continuous and Jumpwise inputs

  • Lim Kyung Eun;Baek Jee Seon;Lee Eui Yong
    • Proceedings of the Korean Statistical Society Conference
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    • 2004.11a
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    • pp.123-128
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    • 2004
  • A finite dam under $P_{\lambda,;,T}^M-policy$ is considered, where the input of water is formed by a Wiener process subject to random jumps arriving according to a Poisson process. Explicit expression is deduced for the stationary distribution of the level of water. And the long-run average cost per unit time is obtained after assigning costs to the changes of release rate, a reward to each unit of output, and a penalty which is a function of the level of water in the reservoir.

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Wastewater Treatment by Microorganism (미생물에 의한 발효처리)

  • ;Kunisuke Ichikawa
    • Microbiology and Biotechnology Letters
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    • v.8 no.2
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    • pp.135-142
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    • 1980
  • The process of biological treatment of organic wastewater is principally associated with those of self-purification in the natural water environment. The treatment system has e intensive function of stabilizing wastewater more effectively than in natural water, which is like natural water concentrated in a small space. Biological treatment of wastewater involves activated sludge and various modified process, trickling filter, rotating disk, oxidation ditch, etc. for aerobic decomposition and anaerobic processes such as anaerobic decomposition and methane fermentation. The basic characteristic of these processes is the use of mixed culture for the conversion of pollutants. This review forcuses on the various kinds of microorganisms related to each treatment processes. Kinetic analysis of the activated sludge process is discussed in order to understand the basis of control and maintenance of the biological treatment process.

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A Study on Recycling NaOH from Pre-treatment Process with Concentration Control System - Scouring Ability of Cotton Fabric Treated with Recycled NaOH - (농도제어장치를 이용하여 면직물 전처리 공정에서 발생하는 가성소다 폐액의 재활용에 관한 연구 - 재활용 가성소다에 의한 면직물의 정련성 -)

  • Lee, Un-Pill
    • Fashion & Textile Research Journal
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    • v.6 no.3
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    • pp.393-398
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    • 2004
  • This research offers recycling method of NaOH from mercerizing process of cotton fabric. The measuring system of NaOH concentration was designed for the mercerizing process and tested for various conditions which can be occurred in factory. The accuracy of the system was varied as the testing condition was changed. As the concentration of sulfuric acid used for titrating NaOH decreased, the accuracy of measuring system increased. The concentration of NaOH for waste water collected from mercerizing process was measured by 5.2%. As the ratio of newly mixed NaOH increased, moisture regain. water absorbency and whiteness of the specimen increased. The bending rigidity(B) and shear rigidity(G) decreased, as the ratio of newly mixed NaOH increased.

On the Microbial Contamination in Softdrink Manufacturing Process (청량음료의 미생물 오염에 대하여)

  • 김용배;이병국;유건희;조남선
    • Korean Journal of Microbiology
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    • v.11 no.3
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    • pp.129-133
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    • 1973
  • The authors have investigated about the microbial contamination of goods which is a criterion of hygienic control. Conducting on investigation, a special attention has been paid on the rate of microbial contamination in the goods, especially in manufacturing process of the softdrink. The authors also made an experiment on total microbes which is the criterion of contamination in each step of the process and in raw materials together with materials to be used for subdividing. Results obtained were as follows : 1) The orgin of microbial contamination was found in bottle cap and in tap water, that is, there appeared 9 colony per ml in bottle cap and 31-74 colony per ml in tap water, respectively. 2) It was found that microbial contamination are 4 colony per ml in average through year. However, it appeared 1 colony per ml in winter and 8 colony per ml in summer. 3) Coliform groups are not detected in goods through a year. 4) There was no variation in number of total microbes after ion exchange resin passage in purification process of tap water. 5) The number of microbes in goods are decreased when the raw materials are treated in high temperature short time (HTST) sterilization.

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Effect of Organic wax residues and particles removal by DIO3 (ozonated DI water) after Silicon Wafer batch Polishing Process (오존수를 이용한 실리콘 웨이퍼 연마 후 지용성 왁스 및 오염입자 제거의 영향)

  • Yi, Jae-Hwan;Lee, Seung-Ho;Kim, Tae-Gon;Park, Jin-Goo;Lee, Gun-Ho;Bae, So-Ik
    • Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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    • 2007.06a
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    • pp.558-559
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    • 2007
  • A commercially de-waxer which kinds of solvent after was used to remove a thick organic wax film after polishing process and several steps of SC-1 cleanings were followed for the removal of organic wax residues and particles which requires long process time and high cost of ownership (COO). DIO3 was used to remove organic wax residues too achieve low COO. In this study, 0103 rinsing could use instead of 01 water rinsing. The process time and chemical consumption were reduced by using DIO3.

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Optimization of the Water Absorption by Crosslinked Agar-g-Poly(acrylic acid) (Agar 그래프트 폴리아크릴산 겔의 흡수능 최적화)

  • Wuttisela, Karntarat;Panijpan, Bhinyo;Triampo, Wannapong;Triampo, Darapond
    • Polymer(Korea)
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    • v.32 no.6
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    • pp.537-543
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    • 2008
  • Crosslinked agar-g-poly(acrylic acid) (x-agar-g-PAA) super absorbent with a water absorbency ($Q_{H2O}$) of approximately 660 g/g was synthesized by the copolymerization of agar with an acrylic acid monomer. KPS and MBA were used as the initiator and crosslinker, respectively. Grafting was performed in air. Infrared spectroscopy was used to identify the product of copolymerization. The optimum conditions to synthesize the x-agar-g-PAA superabsorbent were 0.1 g of agar, 0.1 g of the KPS initiator, for 15 min; 50% AA monomer, 0.005 g of the MBA crosslinker, for a propagation time of 5 min; and 1 M NaOH for 15 min to allow for saponification. The reaction temperature was $80{^\circ}C$.