• 제목/요약/키워드: $A^2/O$ Pilot Plant

검색결과 57건 처리시간 0.026초

농산폐자원의 미생물학적 이용에 관한 연구 (제8보) 섬유질단세포단상질 생산의 시험공장조업 (Studies on Microbial Utilization of Agricultural Wastes (Part 8) Pilot Plant Operation for the Production of Cellulosic Single Cell Protein)

  • 고영희;이계준;배무
    • 한국미생물·생명공학회지
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    • 제5권3호
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    • pp.119-125
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    • 1977
  • 섬유소 단세프 단백질의 대량생산 시험을 위하여 pilot plant 규모의 시험공장 연구를 수행하였는바 그 결과를 요약하면 다음과 같다. 1) 시험공장에서 균체생산을 위한 최적 조건을 pH 7.4, 온도 34$^{\circ}C$, 교반량 130rpm, 통기량 0.4~0.6VVM이었다. 2) 최적배양 조건에서 배지의 적정 수준은 기질로서 볏짚이 4%, (NH$_4$)$_2$SO$_4$0.2%, $K_2$HPO$_4$0.05%, KH$_2$PO$_4$0.10%, NaCl 0.2%, MgSO$_4$ㆍ7$H_2O$ 0.01%, CaCl$_2$ㆍ2$H_2O$ 0.01%, C. S. L. 0.02%였다.

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전해 이산화망간 제조에 관한 연구 (A Study on the Preparation of Electrolytic Manganese Dioxide)

  • 권이묵;김재원;지응업;신종주
    • 대한화학회지
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    • 제17권4호
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    • pp.306-313
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    • 1973
  • 국산 rhodochrosite 로부터 제조한 황산산성 $MnSO_4$ 수용액을 전해산화하여 건전지용 ${\gamma}-MnO_2$를 제조하는데에 관한 공업적 데이터를 얻기 위하여 하루에 4kg의 $MnO_2$를 제조할 수 있는 micro pilot plant를 설치하여 실험하였다. 광석의 침출 및 전해산화 조건을 규명하고 제품의 물성을 화학분석, DTA, X-선회절, 전자현미경사진 및 전지방전 실험 등으로 검토하였다. 적합한 전해조건은 다음과 같다. 전해액의 온도 : $90^{\circ}C$ 이상, 전류밀도 : 0.7${\sim}A/dm^2$, 양극재료 : 흑연 또는 납, 전해액의 농도 :$MnSO_4 50{\sim}150g/l $$H_2SO_4/MnSO_4 = 0.15{\sim}0.25$. 최적전해조건하에서 전류효율은 99%이었고 생성된 $MnO_2$는 거의 순수한${\gamma}-MnO_2$이었으며, 방전특성은 우수하였다.

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돈 슬러리 발효증발 퇴비화 시스템의 온실가스 배출량 측정 (Measurement Emission of Greenhouse Gases from Composting Process for Pig Slurry)

  • 박치호;윤태한;감재환
    • 한국축산시설환경학회지
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    • 제7권2호
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    • pp.111-118
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    • 2001
  • This study was performed for measuring the emission of greenhouse gases, $CH_4,\;N_2O$, from the composting process for pig slurry. For the experiment the benchscale pilot plant was designed by 1$m^3$ volume reactor with a closed type and operated; sawdust 142kg filled before input slurry, slurry about 10~20l inputed per day (total 380l), air supplied 5l/min for 24 hours, mixing time 10 min./day and 1 time a day. From the total experiment period(30days), the amount of VS degradation and emission $CH_4$, $N_2O$ were 10.9kg-VS and 1,582.4g-$CH_4$, 68.1g-$N_2O$ respectively. Based on VS inputed the emission of $CH_4$, $N_2O$ were 15.3(g-$CH_4$/kg-V $S_{input}$), 0.7(g-$N_2O$ /kg-V $S_{input}$), and based on VS degradated were 145.2(g-$CH_4$/kg-V $S_{removed}$), 6.2(g-$N_2O$ /kg-V $S_{removed}$).

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디지털 조속기 시스템의 신뢰성 향상에 관한 연구 (A Study on the Reliability Improvement of Digital Governor System)

  • 신천기;전일영;신남식;하달규;안병주;황춘석;노창주;김윤식
    • 한국정보통신학회:학술대회논문집
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    • 한국해양정보통신학회 1999년도 춘계종합학술대회
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    • pp.375-381
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    • 1999
  • In this study, turbine speed control algorithm is studied for Buk-Jeju steam turbine power plant and also digital governor system is designed for speed control of steam turbine in power plant. By using duplex I/O module, triplex CPU module, 2 out of 3 voting algorithm and adding self diagnostic ability, the reliability of the designed digital governor system can be acquired satisfactorily. Designed and manufactured digital governor system is implemented in a pilot steam turbine plant of 0.3kw output power Installed in Korea Maritime University. After a series of experiment the reliability and availability is confirmed and also stable operation is achieved.

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생물난분해성 유기물질 함유 폐수처리를 위한 Fenton 산화법의 효율적 적용방안에 관한 연구 (A Study on the Efficient Applicability of Fenton Oxidation for the Wastewater Containing Non-biodegradable Organics)

  • 전세진;김미정
    • 상하수도학회지
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    • 제14권1호
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    • pp.76-83
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    • 2000
  • This research is about wastewater containing non-biodegradable TDI(Toluene Diisocyanate) that is treated by the activated carbon adsorption method. In the case of the Fenton oxidation process being applied to the existing process, optimal pH, reaction time, chemical dosing amount, removal rate, and cost were investigated. A pilot plant test was applied after finding optimal conditions with lab experiments. The optimal conditions were pH 3~5(COD removal rate 84~88%) and reaction time 30min~1hr. In higher $H_2O_2$ dosing amount, COD removal rate was a little higher. But there was little difference in the removal rate according to $FeSO_4{\cdot}7H_2O$ dosing amount. Treatment cost was economical in the case of the Fenton oxidation process being operated earlier than activated carbon adsorption system. But chemical dosing point, chemical mixing effect, chemical dosing amount, removal rate, and the cost of facility and others must be considered in practical process.

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$A^2/O$ 공정의 유출수 $NH_4-N$에 대한 모델기반 예측 제어 알고리즘 개발 및 평가 (Development and Evaluation of Model-based Predictive Control Algorithm for Effluent $NH_4-N$ in $A^2/O$ Process)

  • 우대준;김효수;김예진;차재환;최수정;김민수;김창원
    • 대한환경공학회지
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    • 제33권1호
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    • pp.25-31
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    • 2011
  • 본 연구에서는 하수처리공정의 유출 수질을 안정적인 유지하기 위하여, 유입수 패턴을 이용한 모델 기반 $NH_4-N$ 예측 제어 알고리즘을 개발하고 $A^2/O$ 공정을 대상으로 적용 및 평가하였다. 평가에 사용된 자료는 B 시 S 하수처리장에 위치한 pilot 규모의 $A^2/O$ 공정 운전자료를 사용하였다. 생물학적 반응조를 모사하기 위해 수정된 ASM3+bio-P 모델(Lee, 2003)을 사용하였고, 침전조 농도 거동 모사를 위해 일차원 이중 지수 함수 모델(Takacs et al., 1991)을 사용하였다. 유입수 패턴을 이용하여 하루 뒤 유출수 $NH_4-N$ 농도를 예측하고, 사전 작성된 $NH_4-N$ 제어 schedule을 사용하여 pilot plant의 호기조 DO를 조절하는 제어 로직을 적용하였다. 제어 적용성을 평가하기 위해 제어를 적용하지 않은 경우와 적용한 경우를 비교하였고, 계절적 영향을 알아보기 위해 여름철과 겨울철에 $NH_4-N$ 제어 schedule을 적용한 실험을 하였다. 여름철 및 겨울철 모두 제어를 적용하지 않은 경우 수질기준을 초과하는 사례가 발생하였지만, 제어를 적용한 경우 목표수질 이내의 안정적인 유출수질이 방출됨을 확인하였다. 제어를 적용하지 않은 경우에 비교해서, 예측 제어를 적용한 경우에는 송풍기의 RPM이 약 9.1% 증가하였고, 유출수의 $NH_4-N$ 농도는 약 45.2% 감소하였다. 이를 통해 본 연구에서 개발된 유출수 $NH_4-N$ 예측 제어 알고리즘 적용으로 인한 운영비용 증가 대비 수질 개선 효과가 크게 나타났기 때문에, 안정적인 유출수 확보를 위한 측면에서 효율적인 제어기법으로 판단된다.

정수처리에서 미량유해물질 제거를 위한 Peroxone 공정의 적용성 및 경제성 평가 (Evaluation of Applicability and Economical Efficiency of Peroxone Process for Removal of Micropollutants in Drinking Water Treatment)

  • 손희종;김상구;염훈식;최진택
    • 한국환경과학회지
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    • 제22권7호
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    • pp.905-913
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    • 2013
  • We compared the applicability and economical efficiency of peroxone process with those of ozone process in the existing water treatment plant on downstream of Nakdong River. After comparing the peroxone process for removing geosmin with the ozone process in lab scale test, peroxone process showed much higher removal efficiency than the ozone process at the same ozone dosage. Proper range of $H_2O_2/O_3$ ratio were 0.5~1.0 and the half-life of geosmin was about 5.5~6.8 min when the $H_2O_2/O_3$ ratio was set to 0.5 during 1~2 mg/L of ozone dosage. Peroxone process could reduce the ozone dosage about 50 to maximum 30% for the same geosmin removal efficiency compared to the ozone process in the pilot scale test. In case of 1,4-dioxane treatment, peroxone process could have 3~4 times higher efficiency than ozone process at the same ozone dosage. The results of estimating the economical efficiency of ozone and peroxone process for treating geosmin and 1,4-dioxane by using pilot scale test, in case of the removal target was set to 85% for these two materials, the cost of peroxane process could be reduced about 1.5 times compared to ozone process, and in the same production cost peroxone process could have 2~3 times higher removal efficiency than ozone process. The removal efficiency by peroxone process showed a large difference depending on the physicochemical characteristics of target materials and raw water, therefore detailed examination should be carried out before appling peroxone process.

일일 10톤 DME 생산 Demo Plant에서의 분리정제 공정 (SEPARATION AND PURIFICATION PROCESS OF DEMO PLANT FOR 10TON PER DAY DME PRODUCTION)

  • 나영진;조원일;신동근;임계규
    • 한국가스학회:학술대회논문집
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    • 한국가스학회 2005년도 추계학술발표회 논문집
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    • pp.141-145
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    • 2005
  • DME (Di-Methyl Ether) is a new clean fuel and an environmental-friendly energy resource, also is recently increasing with an alternative interest because of the industrial use. DME has been shown to have excellent properties as a diesel fuel giving emission level better than ULEV standard. So it has been attracting considerable as an alternative diesel fuel. In this study, we carried out simulation of separation and purification process of demo plant for 101on per day DME production, which cause the effect that is important in productivity, from operation results of pilot plant for 50kg per day DME production. The liquefied stream, which was separated by gas-liquid separator after DME reactor, includes $CO_2$, DME, Methanol and $H_2O$. We established three distillation columns for separation and purification of the stream. $CO_2$ was extracted from the stream by first distillation column, DME was extracted by second column and Methanol was extracted by third column. We investigated and analyzed the effect which the actual operation variables cause in efficiency of process and optimized process, finally we got the DME of purity $100\%$.

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Screening of Spray-Dried K2CO3-Based Solid Sorbents using Various Support Materials for CO2 Capture

  • Eom, Tae Hyoung;Lee, Joong Beom;Baek, Jeom In;Ryub, Chong Kul;Rhee, Young Woo
    • KEPCO Journal on Electric Power and Energy
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    • 제1권1호
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    • pp.115-120
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    • 2015
  • $K_2CO_3$-based dry regenerable sorbents were prepared by spray-drying techniques to improve mass produced $K_2CO_3-Al_2O_3$ sorbents (KEP-CO2P, hereafter), and then tested for their $CO_2$ sorption capacity by a $2,000Nm^3/h$ (0.5 MWe) $CO_2$ capture pilot plant built for Unit 3 of the Hadong thermal power station in 2010. Each of the sample sorbents contained 35 wt.% $K_2CO_3$ as the active materials with various support materials such as $TiO_2$, MgO, Zeolite 13X, $Al_2O_3$, $SiO_2$ and hydrotalcite (HTC). Their physical properties and reactivity were tested to evaluate their applicability to a fluidized-bed or fast transport-bed $CO_2$ capture process. The $CO_2$ sorption capacity and percentage utilization of $K_2CO_3$-MgO based sorbent, Sorb-KM2, was $8.6g-CO_2/100g$-sorbents and 90%, respectively, along with good mechanical strength for fluidized-bed application. Sorbs-KM2 and KT were almost completely regenerated at $140^{\circ}C$. No degradation of Sorb-KM by $SO_2$ added as a pollutant in flue gas was observed during a cycle test.

합성가스 제조를 위한 CO2/수증기에 의한 메탄 개질반응 연구 (The Study on Methane Reforming by CO2 and Steam for Manufacture of Synthesis Gas)

  • 조원일;이승호;모용기;신동근;백영순
    • 한국수소및신에너지학회논문집
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    • 제15권4호
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    • pp.301-308
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    • 2004
  • The methane reforming with $CO_2$ and steam for manufacture of synthesis gas over $Ni/ZrO_2$ catalyst was investigated. Mixed reforming carried out $CO_2$ dry reforming with $O_2$ and steam for development of DME process in pilot plant. To improve a catalyst deactivation by coke formation, the mixed reforming added carbon dioxide and steam as a oxidizer of the methane reforming was suggested. The result of experiments over commercial catalyst in $CO_2$ dry reforming has shown that the catalyst activity decrease rapidly after 20 hours. In case of $NiO-MgO/Al_2O_3$ catalyst, the deactivation of 20 percent after 30 hours was occurred. The activity of Ni/C catalyst still was not decreased dramatically after 100 hours. The effect of $H_2$ reforming with steam over $Ni/CO_2$ catalyst obtained the optimal conversion of methane and carbon dioxide, and could be produced synthesis gas at ratio of $H_2/CO$ under 1.5.