• Title/Summary/Keyword: Pilot plant test

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A Study on the Applicability of PDA Technique in the P-CAP System for T-P Removal of STP Effluent (하수처리장 방류수의 총인 제거를 위한 P-CAP 시스템에서 PDA 기법의 활용가능성에 대한 연구)

  • Choi, Choongho;Maeng, Sungkyu;Sim, Jaehwi;Choi, Jinho;Song, Kyungguen;Lee, Byungha;Cha, Hoyoung
    • Journal of Korean Society on Water Environment
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    • v.28 no.5
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    • pp.729-742
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    • 2012
  • Recently, to using chemical coagulation process for T-P removal in STP effluent as tertiary treatment process is generalized in the country. The importance of analysis technique to save the treatment & maintenance cost during coagulation process is becoming more increased each day. Thus, it is necessary for the analysis technique during coagulation process to be presented well the characteristic of coagulation in field apply. There are a few analysis techniques such as Jar Test, zeta potential analysis and streaming current detecting techniques. But there are difficult to apply in field immediately due to long test time and difficult analysis techniques. And using PDA technique, it is reviewed applicability of the techniques as field index on pilot plant of P-CAP system The P-CAP system is composed of an in-line static mixer, a Flocculation Tank and the CAP reactor with 2 stage weir for effluent. Pre-test is performed to fix the mixing velocity in the Flocculation Tank using the PDA equipment and it fixed with 30RPM. Also, Jar Test is performed to select optimum dose of each coagulant for each T-P concentration level of influent. Result of continuous test on pilot plant of P-CAP system, the FSI in the Flocculation Tank is increased consistently by increasing each dosing concentration of coagulant such as LAS and PAC in the low level influent T-P concentration comparatively. It is considered that formed Al-hydroxide complexes for dosed coagulant are caused FSI variation. Furthermore, it seems that FSI value in the high level influent T-P concentration appeared lower than the opposite influent condition relatively because it is formed simultaneously Al-hydroxide complexes as solid type and Al-phosphorus complexes as soluble type. Thus, relation of FSI by PDA technique and T-P removal of final effluent on pilot plant of P-CAP system are very limited for the kind of coagulant and the characteristics of influent. And it though that FSI value by PDA technique with analyzing of turbidity in Flocculation Tank will be used restrictedly on field as the relative field-index.

Applicable Feasibility of Fenton Oxidation and Zeolite Ion Exchange Processes for Removal of Non-Biodegradable Matters and Ammonia in Livestock Wastewater (축산폐수 중의 난분해성 물질 및 암모니아 제거를 위한 Fenton 산화와 Zeolite 이온교환 공정의 적용 가능성)

  • Cho, Chang-Woo;Kim, Byoung-Young;Chae, Soo-Choen;Chung, Paul-Gene
    • Journal of Korean Society on Water Environment
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    • v.23 no.5
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    • pp.600-606
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    • 2007
  • Livestock wastewater containing concentrated organic matters and nutrients has been known as one of the major pollutants. It is difficult to apply the conventional activated sludge process to treat livestock wastewater because of high Non-biodegradable (NBD) matter and ammonia. The objectives of this study are to remove NBD matters including aromatic compounds and ammonia in livestock wastewater using Coagulation-Fenton oxidation-Zeolite (CFZ) processes and ascertain applicable feasibility in the field through pilot plant experiment. NBD matters and color remained in the treated water were removed over 92% by Fenton oxidation as the second treatment process. Ammonia was removed by over 99.5% in the zeolite ion exchange process as the last treatment method. From $UV_{254}$, $E_2/E_3$ ratio and GC/MS analyses of treated water at each process, the aromatic compound was converted to aliphatic and aromaticity was decreased. In pilot scale test, organics and ammonia removal efficiencies were not much different from the result of lab-scale test at various operation conditions. Furthermore, reaction time and dosage of Fenton reagent in pilot scale experiment reduced by 40 min and 50% rather than in lab-scale test. $BOD_5$, $COD_{Mn}$, SS, T-N and T-P of treated water in the pilot-scale experiment also met the effluent standards.

Separation of Iron and Nickel from Heavily Concentrated Aqueous Ferric Chloride Solution by Liquid-liquid Extraction (염화 제2철 농축 수용액으로부터의 액-액 추출에 의한 철과 니켈의 분리)

  • Park, Moo-Ryong;Kim, Young-Wook;Park, Jae-Ho;Park, Chin-Ho
    • Clean Technology
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    • v.13 no.4
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    • pp.274-280
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    • 2007
  • A liquid-liquid solvent extraction process was developed in this study to recover Fe and Ni from heavily concentrated aqueous ferric chloride solution, in an effort to substitute the conventional iron reduction method. Solvent composition and extraction conditions were first developed from the laboratory experiments, and the pilot system was designed and built for commercialization. Stage numbers for extraction and stripping were determined from pilot plant runs, and other operation data were obtained for mass production.

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Purification Technology in Closed Water like a Reservoir and Pond using Oxygen Solubilized Device and Standardized Microorganism Culture System (산소용해수와 미생물제재를 이용한 호소 및 폐쇄수역의 정화기술)

  • Seo, Seong-nyeo;Kim, Young-taek;Park, Chul-hwi
    • Journal of Korean Society on Water Environment
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    • v.21 no.2
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    • pp.118-124
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    • 2005
  • The oxygen solubilized device(O.S.D) and standardized microorganism culture system is more efficient than physical and chemical purification techniques in closed water. This study was to determine how the O.S.D and standardized culture system is efficient in purification capacity in closed water based on the lab scale and pilot plant. In the batch test, inducing the quantitative results from pilot plant operation condition, removal efficiency of COD and TN were about 48.3% and 35% respectively, while SS and chlorophyll-a were 94.9% and 68.7%. The pilot plant results showed that suspended solid(SS) and chlorophyll-a removal efficiency were 60% and 59% respectively, due to coagulation characteristics by standardized culture. Total nitrogen(TN) and total phosphorus(TP)showed good effect for the purification of target pond water quality from field data. Additionally, released velocity was determined in control condition of $5.31mgPO{_4}^{3-}{\cdot}m^{-2}{\cdot}day^{-1}$ and $2486.8mgCOD{\cdot}m^{-2}{\cdot}day^{-1}$. Otherwise, phosphate and COD reflux in the aeration and microorganism condition was showed $-9.95mgPO{_4}^{3-}{\cdot}m^{-2}{\cdot}day^{-1}$ and $-397.88mgCOD{\cdot}m^{-2}{\cdot}day^{-1}$. This technology is the most effective not only removal of SS and chlorophyll-a but also control of phosphate and COD release which is very important phenomena in evaluating water quality in closed water like a reservoir and pond.

Development of VR Monitoring System for Gas Plant (가상현실을 이용한 가스플랜트의 VR Monitoring System 개발)

  • Suh, Myung-Won;Cho, Ki-Yang;Park, Dae-You
    • Proceedings of the KSME Conference
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    • 2001.06c
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    • pp.213-218
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    • 2001
  • VR (Virtual reality) technologies have given engineers the ability to design, test, and evaluate engineering systems in a virtual environment. The virtual plant is the highlight of the application of the VR technology to plant engineering. Plant design, maintenance, control, management, operation are integrated in the virtual plant. The VR monitoring system including the concept of the virtual plant is developed to replace a current control room that has number of gages and warning lamps in two-dimensional panels which shows the operating status of a plant. The operating status of the plant is displayed in the VR monitoring system through the realistic computer graphics. Sophisticated, realistic and prompt control becomes possible. The VR monitoring system consists of advanced visualization, walk-through simulation and navigation. In the virtual environment, a user can navigate and interact with each component of a plant. In addition, the user can access the information by just clicking interesting component. The VR monitoring system is operated with various modules, such as (1) virtual plant constructed with Graphic Management System (GMS), (2) Touch & Tell System, and (3) Equipment DB System of Part. In order to confirm the usefulness of the VR monitoring system, a pilot gas plant which is currently being used for plant operator training is taken as application. The end of the paper gives an outlook on the future work and a brief conclusion.

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Risk-based Design of On-board Facility for Lifting System Field Test of Deep-sea Mining System (심해저 광물자원 양광시스템 실증 시험을 위한 위험도 기반 선상 설비 설계)

  • Cho, Su-gil;Park, Sanghyun;Oh, Jaewon;Min, Cheonhong;Kim, Seongsoon;Kim, Hyung-Woo;Yeu, Tae Kyung;Jung, Jung Yeul;Bae, Jaeil;Hong, Sup
    • Journal of Ocean Engineering and Technology
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    • v.30 no.6
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    • pp.526-534
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    • 2016
  • This study had the goal of designing onboard structures for a pre-pilot mining test (PPMT), which is required for the commercialization of the deep-sea mining industry. This PPMT is planned to validate the performance of a hydraulic lifting system and verify the concept of operating through a moon-pool in the east sea, Korea. All of the onboard equipment and facility were designed by KRISO. Because the test was performed at the first development, it is difficult to determine what risk will occur in the facility. Therefore, risk-based design is required in the facility for the PPMT, which includes the facility layout, failure mode and effect analysis (FMEA), and risk reduction plan. All of the expected performances of the lifting system itself and the onboard facilities were qualitatively validated using the risk-based design.

A Study on Kinetic of Volatilization Behavior of Metal Elements Contained in Electric Arc Furnace Dust (전기로 제강분진에 함유된 금속원소의 휘발거동에 대한 속도론적 연구)

  • Yoon, Jaehong;Yoon, Chihyun;Lee, Myungwon
    • Resources Recycling
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    • v.26 no.3
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    • pp.17-25
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    • 2017
  • Electric arc furnace steelmaking dust has various physicochemical properties as volatile components generated in the melting process of steel scraps in an electric arc furnace, which is captured in oxide form as fine powder by reacting with oxygen in the air. In order to efficiently recycle these electric arc furnace dust, a kinetic basic experiment and a pilot production test were carried out in parallel. As a result, it was found that the electric arc furnace dust contain a large amount of Cl and alkali components, thus it was expected that the compounds have a great adverse effect on the actual operation for the recycling. It was confirmed that the volatilization behavior was progressing actively at $1100^{\circ}C$ and the electric arc furnace dust was melted at $1250^{\circ}C$. These results are the same as a result of pilot test for the formation behavior of zinc oxide and reduced iron. These results should be useful as basic data for designing the recycling plant of the electric arc furnace dust and establishing the operating conditions.

Chemical Mechanisms and Process Parameters of Flue Gas Cleaning by Electron beam (전자빔에 의한 배연가스 정화기술의 화학반응 메카니즘에 대하여)

  • Choe, Gap-Seok;Choe, Yeon-Seok;Kim, Han-Seok
    • 연구논문집
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    • s.23
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    • pp.93-107
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    • 1993
  • The chemistry and performance characteristics of the EBDS process have been introduced, in which experimental results from laboratory, test plant, and pilot plant studies agree very well and can be understood from detailed kinetic models. The parametric dependencies of the NOx and $SO_2$, removal yields on the input conditions have been discussed and formulated quantitatively. The process is best suited for flue gas with high $SO_2$, loadings. The operation conditions, such as dose, ammonia, and water additions, can be adjusted fast upon load changes. The process works waste water free and the major product is a mixture of ammonium nitrate and sulfate that can be used as fertilizer. The up-date results show that the EBDS technology is safe and competitive with other already well-established technologies. Due to these interesting features, the electron beam process has gained much international recognition. Demonstration units of 100MW have been proposed in the United States and Japan. Further pilot plants are under construction in Poland and China, countries that make abundant use of highsulfur coal. Additional research activities are under way to further improve the energy efficiency of process, and accelerator prices have been decreasing during the past 10 years. So the EBDS process has a good chance to start a new generation of emission-control technology.

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Decontamination Performance Assessment for the Plasma Arc Vitrification pilot plant on the basis of Trial Burn Results(I) - Decontamination Characteristics for Hazardous Metal, Radioactive surrogate and Radioactive Tracer in Off-gas (시험연소결과에 근거한 플라즈바 아크방식 유리화 시험 설비의 제염성능 평가(I) - 배기가스중의 유해중금속, 방사성핵종 모의물질 및 방사성핵종 제염특성 -)

  • Chae, Gyung-Sun;Park, Youn-Hwan;Min, Byong-Yun;Chang, Jae-Ock;Park, Jun-Yong;Jeong, Weon-Ik;Moon, Byung-Sik
    • Journal of Radiation Protection and Research
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    • v.25 no.2
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    • pp.99-107
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    • 2000
  • Through the results of off-gas analysis at 3 sampling points in Plasma Arc Melting vitrification pilot plant, it was evaluated the partitioning of spiked materials in off-gas and the decontamination characteristic of off-gas treatment system. Spiked materials are hazard_us heavy metals(Pb, Cd, Hg), radioactive surrogate(Co, Cs) and radioactive materials($^{60}Co,\;^{137}Cs$). Through the Trial burn tests, Decontamination factor of spiked materials in off-gas treatment system is calculated.

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Application of Microfiltration and Reverse Osmosis System to Sewage Reuse for Industrial Water (하수를 공업용수로 재이용하기 위한 정밀여과 및 역삼투 시스템 적용에 관한 연구)

  • 강신경;이해군;김지원
    • Membrane Journal
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    • v.12 no.3
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    • pp.151-157
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    • 2002
  • This research was to demonstrate the Possibility of sewage reuse for industrial purpose with use of membrane system. A bench scale test with microfiltration and reverse osmosis showed that microfiltration in the sewage treatment was not able to remove the soluble salts but 70% suspended solids (SS), suggesting that the treated water could be used as direct cooling water. In addition, the reverse osmosis removed not only soluble salts but also 95% SS, proposing that reverse osmosis-treated water could be used as both indirect cooling water and rinsing water. For a 100 ton/day pilot plant, 20 and 12 elements of microfiltration and reverse osmosis were required, respectively.