• Proceedings of the Korean Society for Applied Microbiology Conference
• /
• 1976.10a
• /
• pp.186.3-187
• /
• 1976

섬유소단세포단백의 공업적 생산을 위하여 실험적인 결과를 토대로하여 Jar Fermentor에 의한 scale up 실험을 하였고, pilot plant scale의 발효조를 이용하여 대량생산 실험을 하였는 바 그 결과를 발표하고자 한다. 1. 배양중 생성되는 유기산을 중화하기 위하여 주입되는 암모니아의 소비량과 균체농도는 배양종반을 제외하고는 거의 비례하였으며 암모니아소비량으로 균체생육 정도를 간접적으로 판단할 수 있었다.(중략)

• Journal of Environmental Science International
• /
• v.14 no.8
• /
• pp.771-775
• /
• 2005

The purpose of this research was to investigate applicative possibility of field. Pilot-scale experiments were conducted, at outdoor temperature, HRT l0hour, IR(Internal Recycle) $150\%$ and used $2.8m^3$ Reactor. External carbon source was varied 80 to 120 mg/L. When External carbon source and Alkalinity were injected to the B3 pilot plant, the removal efficiencies of COD and BOD were not decreased. Nitrification rate were 5.95, 5.40, 4.08 $mgNH_4^+-N/gSS/d$ during operation periods and denitrification rate was $3.l2mgNO_3^--N/gSS/d.$ When we surveyed the relationship between loading rate of nitrogen and nitrogen removal quantity, this data was 0.949, B3 process will be possible application process of field.

• Proceedings of the Korea Water Resources Association Conference
• /
• 2015.05a
• /
• pp.283-283
• /
• 2015

1,4-dioxane은 페인트, 광택제 및 코팅제의 제조시에 첨가되는 화학물질로 인간에 대한 발암 가능성과 수중에서의 지속성으로 인해 EPA priority pollutant로 지정되어 있다. 이에 최근 고도산화법을 이용한 처리가 계속적으로 연구되고 있으며, UV/$H_2O_2$ 공법을 통하여 수계에서 발견되는 난분해성 유기 오염물의 제거가 효과적인 것으로 밝혀졌다. 하지만 고도산화공정(AOP)은 다량의 에너지 소모와 산화제 투여로 인한 높은 운전비용이 현실적인 적용에 장애가 되고 있다. 한편 상대적으로 저렴한 비용으로 1,4-dioxane을 처리할 수 있다는 장점으로 인하여 생물학적 분해에 대한 많은 연구가 진행되어 왔다. 하지만, 1,4-dioxane에 대한 많은 연구들이 주로 분해미생물의 분리동정 및 회분식 분해특성에 대한 연구들 위주로 보다 실질적인 연속적 처리반응조의 운전결과들은 거의보고 되지 않고 있다. 본 연구는 Lab scale 연속처리반응조의 장기운전 후 pilot plant 현장적용에 앞서 인공폐수와 합성폐수에서의 분해효율 비교 회분식 실험을 통해 합성폐수내 생물학적 분해에 영향을 미치는 inhibitor의 영향을 확인하였으며, 미생물의 배양 조건에 따른 분해효율 비교 회분식 실험과 modeling을 통하여 현장운영 효율을 예측하였다. 이를 반영하여 추후 진행예정인 pilot plant의 현장 적용성 검토 및 최적 설계인자 도출, 장기운전에서의 효율성 증대를 목적으로 한다.

• Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
• /
• v.7 no.3
• /
• pp.175-182
• /
• 2009

The spent cationic exchange resins and anionic exchange resins were separated from mixed spent exchange resins by a fluidized bed gravimetric separator. The separated resins were identified by an elemental analysis and thermogravimetric analysis. The each test sample was prepared by diluting the slurry made by wet ball milling the cationic exchange resins and the anionic exchange resins separated as a spherical granular form for 24 hours. The resulting test samples showed a slurry form of less than $75{\mu}m$ of particle size and 25,000ppm of $COD_{cr}$. The decomposition conditions of each test samples from a thermal power plant were obtained with a lab-scale(reactor volume : 220mL) supercritical water oxidation(SCWO) facility. Then pilot plant(reactor volume : 24 L) tests were performed with the test samples from a thermal power plant and a nuclear power plant successively. Based on the optimal decomposition conditions and the operation experiences by lab-scale facility and the pilot plant, a commercial plant(capacity : 150kg/h) can be installed in a nuclear power plant was designed.

• Journal of Korean Society on Water Environment
• /
• v.23 no.5
• /
• pp.636-641
• /
• 2007

A pilot-scale biofilm nitiritation reactor was operated with the reject water from a large wastewater treatment plant. The effects of various operating parameters including pH, temperature, dissolved oxygen, solids and organic concentrations were examined. A stable nitritation was achieved at operating pH range of 7.3 to 8.8 with an alkalinity addition. Higher operating temperature of $35{\pm}0.7^{\circ}C$ achieved more stable nitritation compared to $30{\pm}0.2^{\circ}C$. It has been noticed that nitrite accumulation maintained with DO, solids and organic concentrations range of 0.8 to 3.9 mg/L, 3,400 to 11,000 mg/L, and 86 to 572 mg/L, respectively. It seems that the accumulation of nitrite was caused by both the inhibition of $NO_2{^-}$ oxidizers due to free ammonia and the maintenance of the high operating temperature of $35^{\circ}C$ which promote to accumulate the $NH_4{^+}$ oxidizers in the reactor. According to microbial community analysis of fluorescence in situ hybridization and INT-Dehydrogenase measurements, more nitrifiers were presented in attached form compared to suspended growth.

• Journal of Korea Water Resources Association
• /
• v.32 no.3
• /
• pp.311-319
• /
• 1999

Membrane separation process is considered as an alternative of conventional water purification system using coagulationㆍsedimentation＋sand filtration. In this study, it was examined that the application possibility of Hollowfiber Microfiltration membrane for water purification process. A $20m^3/day$ scale pilot plant was used for studying the possibility of long-term operation and the stability of water quality under the optimum conditions, 0.03m/h permeate flux, filtration for 10 minutes, pause for 2 minutes(including air-scrubbing for 30 seconds), obtained by lab-scale experiment. As a result, it was proved stability of pilot plant over one year and filtrate quality(Turbidity. SS etc). Therefore, it was proved that membrane separation process using Hollowfiber Microfiltration membrane can be applied for water purification system

• Korean Chemical Engineering Research
• /
• v.58 no.1
• /
• pp.150-162
• /
• 2020

The proprietary post-combustion CO₂ solvent (KoSol) developed by the Korea Electric Power Research Institute (KEPRI) was applied at the Shanghai Shidongkou CO₂ Capture Pilot Plant (China Huaneng CERI, capacity: 120,000 ton CO₂/yr) of the China Huaneng Group (CHNG) for performance evaluation. The key results of the pilot test and data on the South Korean/Chinese electric power market were used to calculate the predicted cost of CO₂ avoided upon deployment of CO₂ capture technology in commercial-scale coal-fired power plants. Sensitivity analysis was performed for the key factors. It is estimated that, in the case of South Korea, the calculated cost of CO₂ avoided for an 960 MW ultra-supercritical (USC) coal-fired power plant is approximately 35~44 USD/tCO₂ (excluding CO₂ transportation and storage costs). Conversely, applying the same technology to a 1,000 MW USC coal-fired power plant in Shanghai, China, results in a slightly lower cost (32~42 USD/tCO₂). This study confirms the importance of international cooperation that takes into consideration the geographical locations and the performance of CO₂ capture technology for the involved countries in the process of advancing the economic efficiency of large-scale CCS technology aimed to reduce greenhouse gases

• Journal of Wetlands Research
• /
• v.15 no.2
• /
• pp.165-170
• /
• 2013

Pilot scale study was carried out to produce Volatile Fatty Acids with primary sludge from municipal wastewater treatment plant. An acid fermenter was operated at pH 9, $35^{\circ}C$, SRT of 3.5-4.25d, using a final effluent as elutriating water(Mode-I) and pH 9, SRT 5d, temperature of $35^{\circ}C$(Mode-II), $55^{\circ}C$(Mode-III), using a primarily treated water as elutriating water. Although solubilization rate was enhanced with the increase of temperature, the VFAs production rate was decreased. The VS reduction was shown approximately 56%, and the sludge volume reduction was 93%. The optimal conditions for solubilization was obtained at pH 9, $35^{\circ}C$ and SRT of 5d.

• Korean Chemical Engineering Research
• /
• v.50 no.1
• /
• pp.128-134
• /
• 2012

The pilot scale experiments can handle the flue gas up to 1,000 $Nm^3/hr$ for separation of carbon dioxide included in real flue gas at coal-fired power plant. The operational characteristics was analyzed with the main experimental variables such as flue gas flow rate, absorbent circulation rate using chemical absorbents mono-ethanolamine( MEA) and 2-amino-2-methyl-1-propanol(AMP). The more flue gas flow rate decreased in 100 $m^3/hr$ in the MEA 20 wt% experiments, the more carbon dioxide removal efficiency was increased 6.7% on average. Carbon dioxide removal efficiency was increased approximately 2.8% according to raise of the 1,000 kg/hr absorbent circulation rate. It also was more than 90% at $110^{\circ}C$ of re-boiler temperature. Carbon dioxide removal efficiency of the MEA was higher than that of the AMP. In the MEA(20 wt%) experiment, carbon dioxide removal efficiency(85.5%) was 10% higher than result(75.5%) of ASPEN plus simulation.

• 한국신재생에너지학회:학술대회논문집
• /
• 2006.06a
• /
• pp.523-526
• /
• 2006

The target of this work was the process development of demonstration plant to produce the high quailty alternative fuel oil by the pyrolysis of mixed plastic waste. In the first step of research, the bench-scale units of 70t/y and the pi lot plant of 360 t/v had been developed. Main research contents in this step were the process performance test of pilot plant ot 360ton/year and the development of demonstration plant of 3 000 t/y which was constructed at Korea R & D Company in Kimjae City. The process performance of pilot plant of 360 t/v showed components in PONA group appeared at between that of commercial gasoline and kerosene. On the other hand, HO product was mainly paraffin and olefin components and also appeared at upper temperature distribution range than commercial diesel. Gas product showed a high fraction of $C_3\;and\;C_4$ product like LPG composition, but also a high fraction of $CO_2$ and CO by probably a little leak of process.