• Transactions on Control, Automation and Systems Engineering
• /
• 제4권3호
• /
• pp.244-250
• /
• 2002

This paper proposed a modified observer based on Busawon's high gain observer using an appropriate time depended function, which can be chosen to make each estimated state converge faster to its real value. The stability of the modified observer is proved by using Lyapunov function. The modified nonlinear observer is applied to estimate the states in stirred tank bioreactor: out-put substrate concentration, output biomass concentration and the specific growth rate of the process. The convergences of the modified observer and Busawon's observer are compared trough simulation results. As the results, the modified observer converges faster to its real value than the well-known Busawon's observer.

• 제어로봇시스템학회:학술대회논문집
• /
• 제어로봇시스템학회 2001년도 ICCAS
• /
• pp.74.3-74
• /
• 2001

This paper proposes a nonlinear adaptive controller based on back-stepping method for tracking reference substrate concentration by manipulating dilution rate in a continuous baker´s yeast cultivating process in stirred tank bioreactor. Control law is obtained from Lyapunov control function to ensure asymptotical stability of the system. The Haldane model for the specific growth rate depending on only substrate concentration is used in this paper. Due to the uncertainty of specific growth rate, it has been modified as a function including the unknown parameter with known bounded values. The substrate concentration in the bioreactor and feed line are measured. The deviation from the reference is observed when the external disturbance such as the change of the feed is introduced to the system ...

• 한국물환경학회지
• /
• 제21권2호
• /
• pp.132-140
• /
• 2005

The pilot test of a new alternative for small wastewater treatment system has been conducted for two years. It consists of a hybrid bioreactor and the expert system including the process control logic, PLC system, and HMI for the process automation. In order to monitor and remote control its status, the real-time data was transferred from the on-site control center to the central station via a wireless local area network. More efficient and stable performances were observed at automatic operating mode compared with the manual. On an average, COD, SS, T-N and T-P concentrations in the effluent from the hybrid bioreactor were less than 14, 7, 12 and 0.9 mg/L, respectively. According to the result from pilot tests, the quality of treated wastewater with sand filtration was enough to be utilized again.

• KSBB Journal
• /
• 제4권2호
• /
• pp.87-93
• /
• 1989

불용성 기질인 섬유소의 고효율 효소당화에 적합한 분쇄마찰매체함유 반응장치의 개발을 목표로 섬유소-효소-분쇄마찰매체함유 반응장치의 개발을 목표로 섬유소-효소-분쇄마찰매체의 혼합액을 통자체를 회전시켜 교반마찰시키는 tumnling drum type bioreactor를 제작하여 그 효용성을 검토하였다. 반응조 내부의 구조 및 제반 운전조건하에서의 당생성 효울을 분쇄마찰매체의 교반에 소요되는 에너지와 비교분석 검토함으로써 공업적 규모의 활용을 위한 기술적, 경제적 타당성을 평가하였다. 3L규모의 장치의 경우 반응조내경과 baffle의 크기의 비가 1:0.05이고 8개의 baffle을 설치한 반응조에서 3mm glass bead를 600g/l로 첨가하여 100rpm으로 교반할 때 가장 우수한 결과를 얻었다. Tumbling drum type bioreactor는 매우 효율적인 attrition coupled된 당화장치로 판단되며, 특히 산업적 규모로 scale-up하기 용이한 구조를 갖고 있어 이에 대한 구체적 연구가 요망된다.

• Mycobiology
• /
• 제30권4호
• /
• pp.228-232
• /
• 2002

This study focused on the production of high quality compost for the growth of aero-thermophilic fungi, which has a promoting effect on the growth rate and production of oyster mushrooms. The automated solid-state bioreactor system was designed on the basis of a Three-Phase-One system, which controls the serial steps of prewetting, pasteurization and fermentation processes. High numbers of thermophilic fungi and bacteria were recovered from the mushroom composts prepared by this solid-state bioreactor. The rates of composting process were depended on physical as well as chemical factors. Among these factors, the parameters of moisture content and temperature were found to be particularly important. In our automated system, constant levels of moisture content, temperature and ventilation via mixing were provided by a centralized control apparatus including PLC, water tank and water jacket systems. These features induced higher microbiological activity of aero-thermophiles.

• Environmental Engineering Research
• /
• 제22권2호
• /
• pp.210-215
• /
• 2017

Produced water is the largest wastestream of oil and gas exploration. It consists of various organic and inorganic compounds that hinder its beneficial use. This study compared the treatment of produced water in a batch suspended and biofilm activated sludge process. The biofilm carrier material was made from Gardenia Carinata shell. COD, $NH_4{^+}-N$ and $NO_3-N$ removal was monitored in both the suspended (control) and floating carrier bioreactors. The results show a rapid reduction of produced water constituents in the floating carrier bioreactor. COD, $NH_4{^+}-N$ and $NO_3-N$ removal was in the range of 99%, 98% and 97% for the floating carrier bioreactor whereas it was 88%, 84% and 83% for the control bioreactor. The rapid reduction of COD, $NH_4{^+}-N$ and $NO_3-N$ clearly indicate that the floating carrier materials served as an attached growth medium for microorganisms, improved the breakdown of produced water constituents and reduced inhibition of microbial metabolic activities.

• 한국물환경학회지
• /
• 제18권2호
• /
• pp.141-150
• /
• 2002

Two-stage membrane bioreactor using submerged hollow fiber membrane was applied in laboratory scale to treat nitrogen and phosphorus of domestic wastewater. Alum as the flocculant and adsorbent was added into the anaerobic basin of two-stage membrane bioreactor and mixed liquid of aerabic basin was recycled to the anaerobic basin for the purpose of nitrogen removal. Experiment was carried out to find removal efficient of phosphorous and nitrogen components in the mixed liquid, and the stability of the permeate flux and pressure of two-stage membrane bioreactor. In case of alum was added as the flocculant and adsorbent into the anaerobic basin, soluble phosphorus removal efficient was relatively higher and total permeate resistance(Rtot) was more increased out nitrogen removal efficient was lower as the result of lack of alkalinity and insufficient nitrification process than the case of alum was not added.

• Environmental Engineering Research
• /
• 제17권2호
• /
• pp.59-63
• /
• 2012

This paper proposes a modified Ludzack-Ettinger (MLE) type membrane bioreactor (MBR) as a method of treatment for wastewater from food waste disposer. Micro-membrane filtration allows for an extremely low concentration of suspended solids in the effluent. The effluent of the reactor in question is characterized by a relatively high level of non-biodegradable organics, containing a substantial amount of soluble microbial products and biomass. Results obtained in this paper by measurement of membrane fouling are consistent with biomass concentration in the reactor, as opposed to chemical oxygen demand (COD). The MLE process is shown to be effective for the treatment of wastewater with a high COD/N ratio of 20, resulting in are markedly high total nitrogen removal efficiency. Denitrification could be improved at a higher internal recycle ratio. Despite the low concentration of influent phosphorus, the phosphorus concentration of the outflow is seen to be relatively high. This is because outflow phosphorous concentration is related to COD consumption, and the process operates at along solids retention time.

• Korean Membrane Journal
• /
• 제3권1호
• /
• pp.32-38
• /
• 2001

Using the hollow fiber membrane module in a lab-scale membrane bioreactor, the anoxic- oxic (AO) process for nitrogen removal was operated for about one year. For the influent wastewater containing 1,200-1,400 mg $1^{-1}$ of CODcr and 200-310 mg $1^{-1}$ of nitrogen, this process achieved a high quality effluent of less than 30 mgCOD $liter^{-1}$ and 50 mgN $liter^{-1}$. The removal rate of organics was above 98% at a loading rate larger than 2.5 kgCOD $m^{-3}$$d^{-1}$. When the internal recycle from the oxic to the anoxic reactor changed room 2n to 600% rout the influent flow rate, the nitrogen removal rate increased from about 70 to 90% at a loading rate of 0.4 kgT-N m-s d-1. The initial increase of transmembrane pressure (TMP) was observed after a 4-month operation while maintaining the flux and MLSS concentration at 7-9 1 $m^2$ $h^{-1}$ and 6,000-14,000 mg $1^{-1}$, respectively. The TMP could be maintained below 15 cmHg for an 8-month operation. The chemical cleaning with an acid followed by an immersion in an alkali solution gave better cleaning result with the membrane operated for 10 month rather than that only by an alkali immersion.

• 공업화학
• /
• 제17권5호
• /
• pp.521-526
• /
• 2006

폐수를 재이용하기 위한 고도처리 시스템으로서 분리막 생물반응조(Membrane Bioreactor, MBR)는 기존의 활성슬러지 공정(Activated Sludge Process, ASP)에 비하여 많은 장점을 가지고 있다. 도시 하수 중에 포함된 유기물과 영양염류를 동시에 제거하기 위하여 침지형 정밀여과(Microfiltration, MF) 막을 이용한 무산소/호기(Anoxic/Oxic, A/O)형 MBR에서 투과플럭스를 $10.2L/m^2{\cdot}h$로 일정하게 유지하면서 고형물 체류시간(Solids Retention Time, SRT) 변화에 따른 막 여과 특성을 조사하였다. 실험 결과, SRT를 증가시킬수록 체외고분자물질(Extracellular Polymeric Substances, EPS)내 단백질/탄수화물(Protein/Carbohydrate, P/C) 비가 높아져서 막 오염이 빠르게 진행되었다. A/O MBR에 RO막을 결합한 A/O MBR-RO 공정을 폐수의 고도처리에 적용하고자 하였으며, 성능평가를 위해 A/O MBR-RO 공정과 기존의 활성슬러지 공정에 MF와 RO막을 결합한 ASP-MF-RO 공정의 유기물 및 영양염류 제거율을 비교하였다. 실험 결과 A/O MBR-RO 공정이 ASP-MF-RO 공정보다 더 우수한 처리효율을 나타내었다.