• 상하수도학회지
• /
• 제23권6호
• /
• pp.769-778
• /
• 2009

Performances and internal behaviors of the upflow hybrid anaerobic filters treating a dairy wastewater were analyzed to identify the functions and roles of the modular crossflow media and sludge bed layer and to discover their interrelationship in the filter. The media could perform independent biological and physical separation role without buildup of sludge bed, while the role of sludge bed was dependent on the function of the media. The filter packed with the crossflow media did not necessarily require the formation of sludge bed when treating a dairy wastewater. Biological contribution of the media was controlled by that of biologically active sludge bed complementing mutually each other. The gas-liquid-solid separation capability of the media was indispensible to ensure the active biological role of sludge bed, since sludge bed buildup without the media had no independently effective biological function. It was believed that the filter in itself could also function as a selector for physical gas-liquid-solid separation resulting in selectively concentrating particles with superior settleability in sludge bed. The sludge bed in the filter played a key role in the physical solids capture from influent as well as biological organics removal.

• 한국기후변화학회지
• /
• 제7권2호
• /
• pp.103-110
• /
• 2016

In this study, we researched the characteristics of $CH_4$ and $N_2O$ emission of the wastewater treatment (WWT) process in the dairy industry. For flux measurements at the air-water interface, a floating dynamic flow-through chamber was used above the water surface. $CH_4$ and $N_2O$ concentration from the WWT process was measured by NDIR (Non-Dispersive Infrared) Analyser. In the study, $CH_4$ and $N_2O$ fluxes results showed a distinct difference for each WWT process. 60% of the GHG emissions which was the highest percentage were from the equalization tank. Reactor tank was second with 27% of the total emissions from the WWT. Aeration tank was third with 12% of the total emissions. The tendency was that the more the wastewater was treated, the less GHGs were emitted. $CH_4$ and $N_2O$ showed the same tendency. This indicates that the concentrations and properties of wastewater could affect the tendency.

• Journal of Electrochemical Science and Technology
• /
• 제12권1호
• /
• pp.101-111
• /
• 2021

To improve the potential of single chamber microbial fuel cells (SCMFCs) as an applicable technology, the main challenge is a practical application for larger scales bioenergy production from potent exoelectrogenic microorganism with real dairy wastewater. To increase power generation, three individual MFCs were together operated in series best under the fed batch condition for 15 days. The volume of MFC 1 and MFC 2 is "300 mL" and MFC 3 is "500 mL" respectively. The individual MFCs 1, MFC 2 and MFC 3 gives an open circuit voltage of 0.60 V, 0.66 V and 0.55 V and result in total working voltage when connected in series of 1.745V, which lead an LED to glow. The maximum power densities obtained from MFC 1, MFC 2 and MFC 3 are 62 mW/㎡, 50 mW/㎡ and 45 mW/㎡ (normalized to the surface area of the anodic electrode, which was 50 ㎠ for all three MFCs), and corresponding to current densities of 141 mA/㎡, 155 mA/㎡ and 123 mA/㎡, respectively. Therefore this work suggests the cheapest way to connect microbial fuel cells in series to gain power with the lowest operating cost and chemical oxygen demand (COD) removal.

• 한국초전도ㆍ저온공학회논문지
• /
• 제23권3호
• /
• pp.20-25
• /
• 2021

Milking parlor wastewater contains high concentration suspended solid (SS), nitrogen, and/or phosphate as well as organic compounds. A new biological wastewater process by magnetic separation, magnetic activated sludge (MAS) process, was applied to milking parlor wastewater treatment process. A three step wastewater treatment process of coagulation sedimentation / ammonia stripping (C/S), magnetic activated sludge process and contact oxidation (CO) was proposed for removal of these pollutants. First step, C/S process recovered 96% TN and 96% PO₄^3--P as resource for fertilizer from the wastewater. 81% biochemical oxygen demand (BOD) in wastewater was removed after MAS process. As a results, all pollutant concentrations satisfied Japanese effluent standards. Most of residual BOD and SS were removed by the CO process. It was estimated that the proposed process could reduce the process space to 1/7.

• 유기물자원화
• /
• 제3권2호
• /
• pp.37-45
• /
• 1995

유가공폐수 처리를 위한 UASB 의 성능과 운전상의 문제점을 조사하였다. 인공 유가공폐수는 부하3.9kg $COD/m^3.day$까지 성공적으로 운전이 가능하였으며, 이 때 90% 이상의 COD 제거율과 단위 체적당 1.23 I/I.day 의 가스가 발생하였다. 그러나, 부하 2.1kg $COD/m^3.day$ 에서는 침전부 표변에 스컴층이 형성되면서 슬러지부상과 유실이 관찰되었다. 혈청병 (SBT) 실험으로 측정된 우유공장 실폐수와 아이스크림폐수의 생화학적 메탄생성능(BMP) 은 각각 0.135, 0.66ml $CH_4/mg\;COD_{added}$이었다. 반응조의 슬러지 활성도는 식종 초기에 0.159g $COD-CH_4/g$ VSS.d 에서 운전 90 일이 경과하는 동안에 8배 이상 증가하였다.

• 한국초전도ㆍ저온공학회논문지
• /
• 제23권3호
• /
• pp.32-36
• /
• 2021

Milking parlor wastewater contains not only high concentrations of organic compounds, but often animal antibiotics. To discharge the antibiotics to public water area cause problem of antibiotics resistant bacteria. Magnetic separation was applied into improvement of milking parlor wastewater treatment process. A new process, composed of a magnetic activated sludge (MAS) process and a contact oxidation (CO) process, was proposed in this study. This process was evaluated by the simulated milking parlor wastewater (4500 mg/L COD_Cr and 10 mg/L tetracycline) using a bench scale experimental setup. As a result, the process was able to removed 97% COD_Cr as well as 94% tetracycline. The MLVSS (mixed liquor volatile suspended solids) concentration of MAS was maintained at 12000 mg/L without excess sludge drawing. This process was considered to be useful as treatment process for milking parlor wastewater in which waste-milk including antibiotics is often discharged.

• 한국축산시설환경학회지
• /
• 제7권2호
• /
• pp.77-82
• /
• 2001

This research was carried out to investigate the daily amount and characteristics of wastewater produced from bucket milkers, pipeline, tandem ad herringbone milking system for washing operations after milking included 28 dairy farms. The average amount of wastewater produced from milking system was 9.8l/head/day. The amount of wastewater varied from a low of 8.2 litters/head/day(pipeline milking system) to 13.4 litter/head/day(herringbone milking system). The moisture content, Biochemical Oxygen Demand($BOD_5$), Chemical Oxygen Demand($COD_{Mn}$), Suspended Solids(SS), Total Nitrogen(T-N) and Total Phosphorus(T-P) concentration of wastewater were 99.9%, 394mg/l, 417.3mg/l, 1,201.3mg/l, 3.78mg/l, 0.51mg/l.

• Membrane and Water Treatment
• /
• 제9권5호
• /
• pp.335-342
• /
• 2018

Micelle-Enhanced Ultrafiltration (MEUF) is a membrane separation processes that improving ultrafiltration process with the formation of micelles of the surface active agents. Surface active agents are widely used to improve membrane processes due to the ability to trap organic compounds and metals in the treatment of industrial waste water. In this study, surface active agents are used to improve micelle-enhanced ultrafiltration (MEUF) to reduce chemical oxygen demand (COD), total dissolved solid (TDS), turbidity and clogging the membrane in dairy wastewater treatment. Three important operational factors (anionic surface active agent concentration, pressure and pH) and these interactions were investigated by using response surface methodology (RSM) and Box-Behnken design. Results show that due to the concentration polarization layer and increase the number of Micelles; the anionic surface active agent concentration has a negative effect on the flux and has a positive effect on the elimination of contamination indices. pH, and the pressure have the greatest effect on flux. On the other hand, it could be stated that these percentages of separation are in the percentages range of Nano-filtration (NF). While MEUF process has higher flux than NF process. The results have been achieved at lower pressure while NF process needs high pressure, thus making MEUF is the replacement for the NF process.

• 한국환경보건학회지
• /
• 제32권1호
• /
• pp.96-101
• /
• 2006

Chlorination inhibition on the organic removal activity of activated sludge microorganism was investigated in this study. It is well known that chlorination improves the settleability of filamentous bulking sludge through the selective impediment of filamentous microorganisms. However, it is based on the declination of effluent water quality after actual chlorination in dairy wastewater treatment plant. In case of the activated sludge which was exposed in the suggested concentration of chlorine $7.5\;mgCl_2/gVSS/day$ for the filamentous bulking control, decrease of organic uptake rate of $4.9\~24.0\%$, and dentrification rate of $24.8\~30.3\%$ ware shown in comparison to the control group which was not reacted with chlorine. As a result of comparing floc size of activated sludge microorganism, the average of floc diameter in the chlorine exposed group was $150\;{\mu}m$, which displays $25\%$ decrease compared with the control group.

• 한국산학기술학회논문지
• /
• 제9권6호
• /
• pp.1733-1738
• /
• 2008

고농도 유가공폐수의 유기물 및 질소, 인의 제거효율을 비교하기 위하여 두 개의 반응 시스템을 구성하였다. 하나는 하나의 RBC 반응조와 3단 점감포기조로 구성한 시스템이며 다른 하나는 RBC 반응조 2개를 연속으로 구성하고 3단 점감포기조로 구성한 시스템이다. 본 연구에 적용한 바실러스 미생물은 RBC의 끈상미생물접촉재에 부착하여 수행하였다. 각 시스템으로 유입되는 유가공폐수의 BOD 평균농도는 988mg/L, 1,046mg/L이었으며, 유출수 BOD 농도는 21.4mg/L, 15.9mg/L로 제거율은 97.8%, 98.5%의 결과를 보였다. RBC 단일공정 유입수의 평균 $COD_{cr}$ 농도는 1,837mg/L, 유출수는 53.0mg/L로 96.7%의 제거 효율을 보였으며 RBC 연속공정 유입수의 평균 $COD_{cr}$ 농도는 1,852mg/L, 유출수는 평균 27.8mg/L로 98.5%의 제거효율을 보였다. 유입수 T-N 분석결과 RBC 단일공정은 평균 51.9mg/L로 측정되었고, RBC 연속반응공정에서의 유입수 평균은 54.3mg/L이었으며, 유출수는 각각 6.6mg/L, 4.7mg/L로 87.2%, 91.3%의 제거효율을 보였다. T-P에 대한 RBC 단일공정과 RBC 연속공정에서의 분석 결과 유입수 평균농도는 각각 8.9mg/L, 9.1mg/L로 측정되었고, 유출수 농도는 1.6mg/L, 1.0mg/L로 T-P 제거율은 82%, 89%로 나타났다.