• Title/Summary/Keyword: Off-Gas Treatment System

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A Case Study on Operation of Off-Gas Treatment System of Radioactive Waste Vitrification Facility (방사성폐기물 유리화설비의 배기가스 처리계통 운영 사례 연구)

  • Lee, Hye Hyun;Park, Kyu Won
    • Journal of Korean Society of Environmental Engineers
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    • v.38 no.5
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    • pp.249-254
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    • 2016
  • In this study, we investigated the main characteristics of off-gas generated from melting process and off-gas treatment system operation example to provide some primary data for commercial vitrification facility design. The purpose of vitrification facility operation is to treat hazardous materials in the radioactive wastes and harmful off-gas containing a variety of chemical species generated in the glass melting process. Constructing and operating vitrification facility essentially need to be licensed through safety analysis; it is very important to treat radionuclide and hazardous materials below the legal environment emissions regulation level. We must accurately understand the characteristics of off-gas and apply an appropriate off-gas treatment process accordingly. Thus, to design the appropriate off-gas treatment there must be a wide range of elements taken into account such as characteristics of waste and melter, regulation guidance of off-gas, characteristics of generated off-gas and off-gas treatment system performance assessment.

Evaluation of 0ff-gas Characteristics in Vitrification Process of ion-Exchange Resin

  • Park, S. C.;Kim, H. S.;K. H. Yang;C. H. Yun;T. W. Hwang;S. W. Shin
    • Nuclear Engineering and Technology
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    • v.33 no.1
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    • pp.83-92
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    • 2001
  • The properties of off-gas generated from vitrification process of ion-exchange resin were characterized. Theoretical composition and flow rate of the off-gas were calculated based on chemical composition of resin and it's burning condition inside CCM. The calculated off-gas flow rate was 67.9Nm$^3$/h at the burning rate of 40kg/h. And the composition of off-gas was avaluated as $CO_2$(41.4%), steam(40.0%), $O_2$(13.3%), NO(3.6%), and SO$_2$(1.6%) in order. Then, actual flow rate and composition of off-gas were measured during pilot-scale demonstration tests and the results were compared with theoretical values. The actual flow rate of off-gas was about 1.6 times higher than theoretical one. The difference between theoretical and actual flow rates was caused by the in-leakage of air to the system, and the in-leakage rate was evaluated as 36.3Nm$^3$/h. Because of continuous change in the combustion parameters inside CCM, during demonstration tests, the concentration of toxic gases showed wide fluctuation. However, the concentration of CO, a barometer of incompleteness of combustion inside CCM, was stabilized soon. The result showed quasi-equilibrium state was achieved two hours after feeding of resin.

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A Study on Economics of Air Stripping Towers and Activated Carbon Adsorption(Multicomponent System) (충전탑 공기 스트리핑과 활성탄 흡착의 경제성에 관한 연구(다중성분계))

  • Yoo, Ho Sik
    • Journal of Korean Society of Water and Wastewater
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    • v.12 no.4
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    • pp.33-42
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    • 1998
  • The optimum design and preliminary cost estimations of air stripping towers ASTs with granular activated carbon adsorption (GAC) systems as the off-gas treatment were done and compared to liquid-phase GAC system. The optimum design and preliminary cost estimations were done for either single or multicomponent systems. A computer program was developed for this study. 15 single compounds and their multicomponent systems were studies. Even with off-gas treatment, AST was generally a less expensive process for treatment of volatile organics than liquid-phase GAC system. Treatment costs of small systems were sensitive to system capacity. Accumulative effect of treatment costs was found in multicomponent systems. The cost of a multicomponent system was highly dependent on the least strippable component in ASTs even with gas-phase GAC or the least adsorbable component in liquid-phase GAC system.

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Oxygen Transfer Efficiencies of A Single Spiral Roll Aeration System by the Off-gas Method (Off-gas Analyzer를 이용한 하수처리장 단일선회류 방식 포기시스템 산소전달 효율의 평가)

  • Park, Bo Hwa;Ko, Kwang Baik;Park, Jae Han;Lim, Se Ho;Shin, Dong Rok;Yun, Hye Jung;Lee, Ji Young;Moon, Tae Hoon
    • Journal of Korean Society on Water Environment
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    • v.22 no.3
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    • pp.534-539
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    • 2006
  • The supply of oxygen for aeration is the largest energy consumer at activated sludge wastewater treatment plants. Replacement of less efficient aeration systems with fine pore aeration devices can save up to 50 percent of aeration energy costs. The purpose of this study was the diagnosis and evaluation of a domestic wastewater aeration system by the off-gas method which had been studied by US EPA and ASCE. For this study, an off-gas analyzer and its hood were made to collect off-gas. Also, a vacuum pump was connected to the analyzer to make suction of off-gas. Experiments were conducted at a domestic activated sludge wastewater treatment plant which had a single spiral roll aeration system installed with P.E tube diffuser. Data on OTE(f), SOTE(pw), OUR, and air flow rate were obtained from these experiments. In case of replacing an aeration system, it is recommended that it should be replaced with perforated membrane disc or ceramic disc fine bubble diffusers installed in a full floor coverage or grid pattern.

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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Development of a Micro-Bubble System for Ozone Off-Gas Recycling in the Ozone Treatment Process (오존처리공정의 배오존 재활용 마이크로버블시스템 개발)

  • Young-Man, Cho;Jae-Ouk, Jung;Kwang-Heon, Lee;Yong-Jun, Jung
    • Journal of Environmental Science International
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    • v.31 no.12
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    • pp.1061-1068
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    • 2022
  • The purpose of this study was to develop a recycling system for ozone off-gas. Although the ozone transmission rate of the injector method differs slightly depending on the ozone injection rate, it reaches approximately 99%, which is very high. During the increase in water inflow to the ozone recycling system from 2 L/min to 10 L/min, the average ozone recycling rate was 99.4% at a 1 ppm ozone injection rate, 98.6% at a 2 ppm ozone injection rate, 98.1% at a 3 ppm ozone injection rate. Ozone treatment facility operating costs can be divided into the costs of pure oxygen production, ozone production, and maintenance. The annual operating costs of ozone treatment facilities in Korea are estimated to be approximately 38.9 billion won. The annual savings are estimated to be approximately 5.8 billion won when the ozone transfer rate of the diffuser method, which is mostly employed in domestic water treatment plants, is 85% and 15% of the ozone is recycled.

Study on the Standard Oxygen Transfer Efficiency Monitoring System in the Aeration Tank for Reuse and Discharge of Wastewater (하폐수의 재사용 및 방류를 위한 폭기조 내 표준산소전달 효율 모니터링 시스템에 관한 연구)

  • Kim, Hong-Seok;Kim, Yong-Beom;Ko, Kyung-Han;Kim, Sang-Woo;Shim, Hwan-bo
    • Resources Recycling
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    • v.28 no.6
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    • pp.73-78
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    • 2019
  • In this investigation, off-gas generated from the activated sludge in wastewater treatment plant was monitored. Through monitoring, the oxygen transfer efficiency in the aeration system and the reliability was evaluated by comparing to clean water. First, the dissolved oxygen, oxygen transfer coefficient, and standard oxygen transfer efficiency were measured based on clean water, and the values were 8.60 mg/L, 9.490/hr and 23.96%, respectively. The off-gas monitoring at the wastewater treatment plant indicated that the standard oxygen transfer efficiency was 22.81%. Little difference in oxygen transfer efficiency this data inferred that the performance was improved through diffuser installation in the field monitoring system.

Evaluation of the Oxygen Transfer Parameters (α and F) of a Coarse Bubble Aeration System by Off-gas Column Test (Off-gas Column Test를 이용한 하수처리장 심층포기시스템의 산소전달 매개변수(α와 F)의 산정)

  • Kim, Chul Woong;Lee, Se Ho;Shin, Dong Rok;Lee, Ji Yong;Park, Jae Han;Ahn, Yoon Hee;Ko, Kwang Baik
    • Journal of Korean Society on Water Environment
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    • v.22 no.6
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    • pp.1119-1122
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    • 2006
  • Aeration by using diffusers usually requires approximately 50~90% of the total electricity needed to operate WWTP (WasteWater Treatment Plant)s. Accurate evaluation of the oxygen transfer efficiency for an aeration system, and recommendation of a better alternative may help saving WWTP operational costs. Appropriate techniques and methods to achieve this purpose have not been introduced in Korea. In this study, in-process analysis was performed for a coarse bubble aeration system by the off-gas method to evaluate its applicability in Korea. To accomplish this analysis, an off-gas test, unsteady-state clean water test and steady-state off-gas column test was conducted and comparisons to other aeration systems were made. The ${\alpha}$ and the F estimated from the results of the unsteady-state clean water test and the steady-state off-gas column test were 0.61 and 0.90 respectively in a coarse bubble aeration system. The comparison of P.E tube diffusers laid out single spiral roll and ceramic dome diffusers laid out full floor coverage showed that the oxygen transfer efficiency of the coarse bubble aeration system was less than or similar to other aeration systems. But, airflow rates per unit area were 4~5 times greater than other aeration systems. In regards to the oxygen transfer efficiency for airflow rates per unit area, a retrofit to higher efficiency diffusers was urgently needed. This study showed proved that off-gas methods can apply to evaluate diffuser performances to estimate operating factors and to compare other aeration systems in Korea.

Greenhouse Gas Emission Analysis by LNG Fuel Tank Size through Life Cycle

  • Park, Eunyoung;Choi, Jungho
    • Journal of Ocean Engineering and Technology
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    • v.35 no.6
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    • pp.393-402
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    • 2021
  • As greenhouse gas emissions from maritime transport are increasing, the International Maritime Organization is continuously working to strengthen emission regulations. Liquefied natural gas (LNG) fuel is less advantageous as a point of CO2 reduction due to the methane leakage that occurs during the bunkering and operation of marine engines. In this study, greenhouse gas emissions from an LNG-fueled ship were analyzed from the perspective of the life cycle. The amount ofmethane emission during the bunkering and operation procedures with various boil-off gas (BOG) treatment methods and gas engine specifications was analyzed by dynamic simulation. The results were also compared with those of other liquid fuel engines. As a result, small LNG-fueled ships without a BOG treatment facility emitted 32% more greenhouse gas than ships utilizing marine gas oil or heavy fuel oil. To achieve a greenhouse gas reduction via a BOG treatment method, a gas combustion unit or re-liquefaction system must be mounted, which results in a greenhouse gas reduction effect of about 25% and 30%. As a result of comparing the amount of greenhouse gas generated according to the BOG treatment method used with each tank size from the perspective of the operating cycle with the amounts from using existing marine fuels, the BOG treatment method showed superior effects of greenhouse gas reduction.