• Journal of the Korea Organic Resources Recycling Association
• /
• v.21 no.2
• /
• pp.71-78
• /
• 2013

This study examined the feasibility of phosphorus removal from dewatering centrate/filtrate in wastewater treatment by struvite formation. Since dewatering centrate/filtrate obtained after anaerobic digestion contains a high content of ammonia, magesium addition and pH adjustment could remove phosphorous. The optimum magnesium dose, reaction time, settling time, and pH value was found at 2 mol Mg/mol $PO_4^{3-}$, 10 min, 120 min, and 8.5, respectively. A bench-scale continuous operation at the optimum condition showed 80% of total phosphorus removal and 82% of phosphate removal in dewatering centrate. The elemental composition and crystal structure of the chemical precipitate was similar to the reported values of struvite.

• Journal of the Korea Organic Resources Recycling Association
• /
• v.16 no.2
• /
• pp.47-56
• /
• 2008

The objective of this research is to evaluate the optimum recycling methods for the sewage sludge cakes at different microwave power-settings and for different periods of time. The dehydrated sewage sludge cakes used in this study was obtained from N wastewater treatment plan in the P City. The beginning drying processes were carried out in a microwave oven with 2,450 MHz frequency and power ranges of 1kW to 4 kW. The continuous conveyer drying system was also operated with 2,450 MHz frequency and power setting, ranging from of 1 kW to 6 kW. Initial moisture content of the sewage cake is 78~80%, and the moisture content decreased rapidly up to 0.2~2(wt%) within short periods due to breaking the cell walls. This study is also conducted to evaluate the characteristics of sewage sludge cakes with respect to important physical parameters effect on the thermal kinetics for evaporation water in the sludge which are operation times, moisture contents, drying rates, input amounts, flow rates and calorific values. It takes 60 minutes and 120 minutes to reach the critical moisture contents with power setting of 4 kW for 3kg/min and 6kg/min of the flow rates respectively. It takes 120 minutes and 110 minutes to reach the critical moisture contents with flow rates of 2.5 cm/min and sludge input of 6kg/min for the power settings of 4 kW and 6 kW respectively. The most effective value of the power for drying the sludge is 4 kW. Operation with 6kg/min and 4kW on 2cm of the sludge thickness can be effectively and inexpensively to reach the critical moisture contents, when you compare 2cm of the sludge thickness with 1cm and 3cm of the sludge thickness.

• Journal of the Korea Organic Resources Recycling Association
• /
• v.16 no.3
• /
• pp.29-37
• /
• 2008

The objective of this research is to evaluate the optimum treatment methods for disposal sludge cake at different temperatures and periods of time. The disposal dehydrated sewage cake used in this study was obtained from N wastewater treatment plant in the P City. This system consists of continuous conveyer thermal dryer and pyrolysis. The continual conveyer thermal dryer was operated to evaluate the optimum conditions with temperature settings, ranges from 130 to $180^{\circ}C$, loading rates of 650~750 kg/hr and operating times of 110~120 minutes. The continual pyrolysis was also operated to evaluate the optimum conditions with temperature settings, ranges from 650 to $750^{\circ}C$, loading rates of 100~158 kg/hr and operating times of 20~40 minutes. The sewage sludge cake has a moisture content of 78~80% (wt) which decreased up to 1~3%(wt) resulted in breaking of cell wall after operating the continuous conveyer thermal dryer and pyrolysis. Important parameters which were operating times, moisture contents, loading rates, conveyer velocities and rotary velocities effects on the thermal kinetics and dynamics were investigated to evaluate the optimum conditions for the continual thermal dryer and pyrolysis.

• Journal of the Korean Recycled Construction Resources Institute
• /
• v.4 no.4
• /
• pp.477-482
• /
• 2016

This study investigates the expressions characteristics of compression strength depending on the condition of fresh concrete and cured concrete by producing Non-cement mortar and concrete only with solidified sludge in the dehydrated cake form, recycled concrete and premixed materials(BS, FA) in order to actively use remicon recycling water as resources, rather than as construction waste material. After treating wastewater of pH 12.5 or more with alkali activator and after promoting BS hydration reaction, the amount of BS inflow was found to be increased and compression strength was increased accordingly: these results coincide with the analysis results of TG-DTA and SEM.

• 한국신재생에너지학회:학술대회논문집
• /
• 2011.11a
• /
• pp.110.2-110.2
• /
• 2011

바이오가스 생산은 현재 정부에서 추진하고 있는 저탄소 녹색성장으로 인해 더욱 그 가치의 중요성이 부각되고 있다. 스웨덴 Scandinavian Biogas Fuel AB(SBF) 사의 바이오 가스 생산 기술을 이용함으로 소화효율을 개선하고 바이오가스 발생량을 극대화하였다. 전국 403개 공공하수처리시설 중 소화조가 설치된 처리시설은 65 개소이며 이중 57 개소에서 총 64개 소화조를 운영 중이다. 하지만 국내 소화조의 효율은 유입수질 저하, 운영, 관리 미숙으로 인해 전진국의 1/4 수준으로 에너지 이용률이 미미한 편이다. 환경부는 2010년부터 에너지 이용, 생산사용 확대, 추진을 위해 하수처리시설별 이용 가능한 에너지 잠재력의 종류, 양, 지역 내 수요자, 공급자 의 현황 규모 등을 정리해 2012년부터 에너지 이용사업 확대를 추진한다. SBF의 기술을 바탕으로 하수처리시설에서 들어오는 하루 슬러지 $1370m^3$와 음식물쓰레기 180t을 함께 처리하며 바이오가스 생산량을 더욱 늘렸다. 각 $7,000m^3$의 달걀모양(egg shape) 소화조 2개를 운영하며 생 슬러지와 음식물 쓰레기 처리 후 바로 소화조로 투입, 혐기 소화하는 방식이며 슬러지 최종처분방법은 탈수 후 소각된다. 반입되는 생 슬러지의 평균 TS 1.7%, VS 63% 이며 농축 후에는 평균 TS 9%, VS 75% 이다. 또 소화조로 들어가는 음식물 쓰레기는 평균 TS 8%, VS 85% 이며 소화 후 평균 TS 3.6% VS 59% 이다. 그리고 소화조의 pH는 7.3~7.8,유기산의 농도는 150mg/L~350mg/L, 가스발생량은 하루 평균 $26,500Nm^3$이며 소화효율은 평균 67%이다. 혐기성소화는 산소가 없는 무 산소 상태 에서 분해 가능한 유기물을 분해시켜 메탄으로 전환시키고 우리는 현재 이 가스를 소화조 가온에 사용하고, 판매하고 있다. 소화효율을 높이기 위하여 가온과 교반이 행해지는데 가온방식은 직접가온방식(증기주입식)과 간접가온방식(열교환방식)이 있다. 그중 우리는 간접가온방식을 채택하여 소화효율을 높였고 일반중온 혐기소화온도보다 약간 높은 $38^{\circ}C$로 운전한다. 그리고 일반적으로 알려진 교반방식인 가스교반, 기계교반, 이 둘은 병행한 교반이 아닌 독자적인 방법을 이용, 소화조 내의 슬러지가 정체되어 교반되지 않는 부분을 최소화 하였다. 이때 미생물이 투입되기 힘든 소화조 아래 쪽 으로도 고루분포 되어 슬러지를 이용 하게 되고 소화조 상하부의 온도차가 $1^{\circ}C$ 이하로 거의 완벽한 교반상태를 보여 줌 으로써 소화효율을 최대한으로 한다. 더욱이 소화일수 부족으로 인한 전반적 소화효율 저하가 발생하지 않도록 input과 output 조절을 통한 적정소화일수 20~25일을 최대한 맞추어 운전하여 소화조 설계용량의 평균 90%를 활용하고 있다.

• Membrane Journal
• /
• v.16 no.3
• /
• pp.182-187
• /
• 2006

The purpose of this study was to investigate effect of coagulation on filtration performance of membrane in submerged MBR system and influence of continuous aeration to reduce fouling of membrane surface on coagulated floc. For this purpose, aeration tank sludge of MBR system was compared with jar-test sludge. The experimental results were analysed in terms of floc size and SRF (Specific resistance of Filtration). The more alum was added, the more content of floc below $10{\mu}m$ reduced and SRF decreased. But compared with jar-test results, it was found that effect of coagulation on MBR floc was reduced. Operation time of membrane in alum added MBR was longer than that in control MBR. But operation time was not proportional to alum dose. It was thought that the result was reason that floc below $10{\mu}m$ was not reduced sufficiently by shear force of continuous aeration. Moreover it was founded that if alum is added more than proper dose, it brings filtration resistance to increase.

• Journal of Energy Engineering
• /
• v.22 no.4
• /
• pp.355-361
• /
• 2013

In this work, torrefaction of the sewage sludge was investigated the characteristics of torrefied products and the value of as energy resource to improve energy density and to maintain consistent quality of SRF. Torrefaction was performed two important torrefaction operational parameter, temperature($150-230^{\circ}C$) and reaction time(10-60min). As raising the torrefaction temperature at long reaction times, the moisture content of torrefied products was decreased, while the heating value was increased. Moreover, increasing of the torrefaction temperature led to a increase of the content of the carbon up to 60% compare to the initial the sample, and a decrease of the content hydrogen and oxygen. Especially, Average heating value was 4,818 kcal/kg regardless of the reaction time when torrefaction was performed over $210^{\circ}C$. In addition, the fuel ration and coal band were improved after torrefaction because the O/C and the H/C ratio were decreased.

• Journal of the Korea Academia-Industrial cooperation Society
• /
• v.17 no.12
• /
• pp.1-8
• /
• 2016

This study assessed the feasibility of odor removal by the application of Bacillus sp. that has many advantages in sewage treatment to sewage sludge. The NH3 removal rates in the treatment of primary sludge using only aeration were measured at 24, 48, and 72 hours of treatment and the results were 12.5 %, 12 %, and 42.1 %, respectively. The NH3 removal rates of a reactor injected with BIO-CLOD made by solidifying Bacillus sp. concentrated 10 % together with other substances were measured after 24, 48, and 72 hours of treatment and the results were 43 %, 70 %, and 81 % respectively. In the cases where the Bacillus sp. cultured in NB medium was injected into the primary sludge reactor to reach injection rates of 0 %, 1.7 %, 3.3 %, and 6.7(v/v%), the TVOC removal rates measured when 72 hours had passed after the injection were 59 %, 71 %, 88 %, and 98 % respectively, which were higher than the NH3 removal rates as the NH3 removal rates measured at the same time were shown to be 29 %, 25 %, 31 %, and 48 %, respectively. In the sludge dewaterability conducted with various Bacillus sp. injection concentrations, a Bacillus sp. concentration of 4(v/v%) was considered to be suitable. The Bacillus sp. concentrations and reduction in the bad odor substances were correlated with each other. The results showed that aeration and Bacillus sp. injection will assist biological oxidation so that the bad odor substances can be removed. Based on the SRF values of the primary sludge and digested sludge, in which Alum and PAC were used, the appropriate amount of Alum aggregate reagent was judged to be 500 mg/L, and when PAC was used, 6 mg/L was judged to be appropriate.

• Journal of the Korean Society for Environmental Technology
• /
• v.19 no.6
• /
• pp.556-562
• /
• 2018

Due to the enforcement of effluent water regulation the advance sewage treatment system is needed to retrofit and remodelling. In this case the most important issue is the effluent concentrations of TP and there are a lot of system to reduce its concentration. But biological treatment processes have many restrictions to enhance the removal efficiency of TP. In this study the efficient ECO operating condition to improve and retrofit biological sewage wastewater treatment system is as follow; 1) The treatment efficiency of BOD, TN and TP at the current density of $15mA/cm^2$ was higher than the treatment efficiency at $5mA/cm^2$ in the electrodes arranged with Al-SUS(Stainless Steel) regardless of the reaction time, The TP concentration was 0.1 mg/L or less. Especially, when the reaction time was maintained at 10 min, the TP concentration was 0.06 mg/L or less irrespective of the current density. 2) The change of TP concentration is not influenced by the change of current density and rather the concentration of treated water changes according to the reaction time. In the case of electro coagulation reaction, a few seconds to several minutes are required. However, the reaction time of electro coagulation and oxidation was studied to be more than 10 minutes. 3) As a result, it has been studied that the economical current density of the electro coagulation oxidation process for TN and TP treatment of domestic wastewater is $15mA/cm^2$ or less and the reaction time is 10 minutes.

• Journal of the Korean GEO-environmental Society
• /
• v.10 no.2
• /
• pp.37-43
• /
• 2009

With the economic development of Korea, sewage treatment facilities and waste food treatment facilities have been steadily increased. These facilities have positive effects such as the conservation of the water resources quality and waste food recycling while they also affect the neighborhood life with severe odor problems. Therefore, it was first collected sludge samples from 5 sewage treatment facilities and 5 waste food treatment facilities where the amounts of waste produced from above sites are relatively immense in Busan and estimate the $H_2S$ emission rates. Then it was selected 1 sample which has the highest emission rate of $H_2S$. Using flux chamber and GC/FPD analyses, it was tried to quantify the emitted amount of sulfonic gas concentration under anoxic condition. The sludge sample obtained from Noksan sewage treatment facility has the highest emission rate of $H_2S$. This sample contained 156.18 mg/kg $H_2S$. The odor compounds were analyzed using GC/FPD and the concentrations were converted to odor quotient. Among odor compounds the ratio of $CH_3SH$ (methylmercaptan) for the total odor quotient was 47.3% and considered to be the main odor compound in the sample.