• 제목/요약/키워드: Distillery Wastewater

검색결과 22건 처리시간 0.024초

주정폐수 처리를 위한 SBR 운전주기에 관한 연구 (A Study on Operation Cycle of SBR for the Treatment of Distillery Wastewater)

  • 최유현;엄한기;김성철;주현종
    • 한국물환경학회지
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    • 제32권2호
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    • pp.191-196
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    • 2016
  • This study aimed to evaluate SBR operation cycle for removing the high-concentration organic matter of distillery wastewater in the ginseng processing plant. The experiment was conducted with the use of a laboratory scale SBR reactor and distillery wastewater as the influent. The results indicated an increase in pH from 4.08 to 7.59 of distillery wastewater after aeration for 2 hours. Also, the optimum SBR operation cycle for the removal of organic matter and nitrogen was 2 hr of aeration and 6 hr of anaerobic conditions. Adjustment of proper pH through aeration time is most critical in the SBR operation for distillery wastewater treatment. In this study, we presented an efficient method for distillery wastewater treatment.

유기산 생산 세균을 고정화학 2상 메탄발효조에 의한 주정 폐수의 고효율 소화 (A Study on the Use of an Immobilized-Cell Acidogenic Reactor for the High Rate Digestion of a Distillery Wastewater)

  • 배재근;고종호;김병홍
    • 한국미생물·생명공학회지
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    • 제22권4호
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    • pp.407-414
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    • 1994
  • Anaerobic fermentative bacteria were isolated from the acidogenic reactor of a labora- tory scale 2-stage anaerobic digestor. The isolate 1-6 was selected for its ablity to produce more fatty acids from distillery wastewater than others, and was identified as a strain of Clostridium. The isolate Clostridium sp. 1-6 is a thermophilic bacterium growing at 55$\circ$c , and grew best at pH 5.5. An acidogenic reactor using immobilized cells of the isolate Clostridium sp. 1-6 removed about 15% of COD from distillery wastwater as hydrogen, producing about 50 mM butyrate and about 10 mM acetate, when the reactor was operated at the hydraulic retention time(HRT) of 0.8 hr. It is proposed that this system can be used to convert the distillery wastewater to hydrogen and butyrate. More than 90% of COD was removed from the wastewater by anaerobic digestion using a 2-stage digestor consisting of a UASB methanogenic reactor and an acidogenic reactor of the immobilized cells of isolate Clostridium sp. 1-6.

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Treatment of Distillery Wastewater Using a Thermophilic High-Rate Hybrid Anaerobic Reactor in Industrial Scale

  • Nam, Ki-Du;Chung, In;Young, James C.;Park, Wan
    • Journal of Microbiology and Biotechnology
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    • 제9권6호
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    • pp.737-743
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    • 1999
  • A conventional thermophilic anaerobic digester was converted into a thermophilic high-rate hybrid anaerobic reactor (THAR) for treating distillery wastewater. The THAR has been operating successfully since May 1995 at a loading rate of 5.45 to $11.52{\;}kg/\textrm{m}^3/d$ (maximum of 15.02). The THAR has demonstrated a soluble Chemical Oxygen Demand (sCOD) removal efficiency of 85 to 91% and a total COD (tCOD) removal efficiency of as much as 72 to 84%. Product gas had a methane content of 59 to 68%. The tCOD removal rates were 4.31 to 5.43, 6.26 to 6.89, and 9.03 to $9.78kg{\;}tCOD/\textrm{m}^3/d$ for tapioca, com, and naked-barley wastewater, respectively. The sCOD removal rates ranged from 3.75 to 4.79,3.28 to 4.89, and 5.57 to 6.21kg $sCOD/\textrm{m}^3/d$ for tapioca, com, and naked-barley wastewater, respectively. There were unknown substances in a naked-barley distillery wastewater that were identified as being toxic for microorganisms. However, the THAR treated naked-barley wastewater continuously for 26 days, operating at an average tCOD loading of $11.08{\;}kg/\textrm{m}^3/d$without any signs of deterioration in either COD removal efficiency or gas production rate. During this period, the average removal efficiencies of tCOD and sCOD were 84% and 91%, respectively, and the gas production rate averaged 6.61 to $7.57{\;}\textrm{m}^3/\textrm{m}^3$ reactor/d which produced 0.57 to $0.69{\;}\textrm{m}^3{\;}biogas/kg{\;}tCOD_{rem}$. From tapioca and com wastewater, the reactor showed an average gas production rate of 3.18 to 3.46 and 4.91 to $5.22{\;}\textrm{m}^3/\textrm{m}^3$ reactor/d which produced 0.53 to 0.69 and 0.62 to $0.71{\;}\textrm{m}^3/kg{\;}tCOD_{rem}$, respectively.

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알콜증류폐액을 이용한 빵효모배양에서 Glucose와 Ammonium의 자동첨가에 의한 종균 : pH-stat 방법에 의한 Ammonium의 자동첨가 (Increase of Cell Concentration by the Automatic Addition of Glucose and Ammonium to an Alcohol distillery Wastewater Reutilized for Cultivating a Baker's Yeast : Automatic Addition of Ammonium with pH-stat)

  • 이형춘
    • KSBB Journal
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    • 제15권2호
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    • pp.134-138
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    • 2000
  • 알콜증류폐액에 빵효모를 배양하는 중에 glucose와 ammo-nium을 자동첨가함으로써 폐액배양액의 균체농도를 높여서 알콜증류폐액의 이용성을 증가시키고자 하였다. 배양중에 glucose를 공급하여 줌으로서 공급하지 않은 경우보다 1.3배 더 높은 균체농도를 얻었으며, glucose와 (NH4)2SO4를 공급하여 줌으로써 5.8배 더 높은 균체농도를 얻었다. Glucose의 경우에는 배양액의 DO를 제어파라미터로 하는 제어방법을 사용하여 자동첨가하고, ammonium의 경우에는 pH조정제로서 NH4OH을 사용함으로서 pH제어기에 의하여 자동으로 공급되도록 배양하였다. 배양결과 증식의 정체없이 배양 22.5시간후에 최대 12.0 g/L의 건조균체량에 도달하였으며, 균의 최대비증식속도는 0.18 hr-1였고, 대당균체수율이 약 0.54g/gdldjTdmamfh glucose의 첨가가 경제적이라고 생각되었다. 증균배양으로 폐액배양액의 COD를 약 22% 더 감소시킬 수 있었다.

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알콜증류폐액을 이용한 빵효모배양에서 포도당, 암모늄 및 인산의 자동첨가에 의한 증균 (Increasing Cell Concentration by the Automatic Addition of Glucose, Ammonium and Phosphate in the Cultivation of a Baker′s Yeast in Alcohol Distillery Wastewater)

  • 이형춘
    • KSBB Journal
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    • 제18권3호
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    • pp.197-201
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    • 2003
  • 알콜증류 폐액에 빵효모를 배양하는 중에 포도당, 암모늄 및 인산을 자동 첨가하여 균체량을 효율적으로 증가시킴으로써 폐액의 재이용성을 향상시키고자 하였다. 포도당은 DO를 제어파라미터로 하는 제어방법을 사용하여 자동 첨가함으로서 그 농도를 300 mg/L 이하로 유지하였다. 암모늄은 pH-stat 방법을 사용하여 N $H_4$OH로서 자동 첨가함으로서 12.6~17.4mM의 낮은 농도범위로 유지하였다. 인산의 경우에는 분석방법으로써 ascorbic acid법을 채택한 자동화 FIA sysetm을 제작하여 사용하였다. 이 system으로 배양 19.4 시간 후부터 배양액을 자동분석하고 제어한 결과 배양액의 P $O_4$-P 농도를 23.3~43.4 mg/L 의 낮은 농도범위로 유지할 수 있었다. 세가지 영양성분을 자동첨가하면서 배양한 결과 증식의 정체없이 균체량을 33.0배 더 증가시킬 수 있었다. 비증식속도는 0.19 $hr^{-l}$였다.

생물학적으로 처리한 주정폐액의 효율적인 화학적 처리방법 (Effective Chemical Treatment of Biologically Treated Distillery Wastewater in Industrial Scale)

  • 남기두;정인;허다니엘;박완
    • 생명과학회지
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    • 제9권6호
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    • pp.692-697
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    • 1999
  • 주정폐액과 같은 고 농도의 유기성 폐액의 효율적 처리에는 혐기적, 호기적인 생물학적인 처리와, 생물학적으로 난분해성 물질의 화학적 처리가 요구되었다. 난분해성 COD성분을 제거하기 위하여 Fenton처리 전에 가능한 많은 유기물의 제거가 요구되며, 이때 $FeCl_3$,alum,cationic polymer의 처리가 효과적이었다. 이 처리과정 중은 몰론 Fenton 처리과정 중에 생성되는 슬러지의 제거 효율에 따라 전체 폐수처리효율리 크게 영향을 받게되 슬러지의 효과적인 제거과정이 필요하였다, 이를 위해 기포의 직경이 80-120 um 정도되는 기존의 DAF방식에 비해 새로 도입한 PBF법에 의해 생성되는 직경 20-50um 의 미세포기는 슬러지의 부상을 촉진시켜 화학적 슬러지의 제거 효율이 훨씬 뛰어남을 알 수 있었다. 이에 따라 PBF법에 의한 슬러지의 제거는 기존의 DAF법에 비해 약품 사용량, 용수의 절감, 방류량의 감소 등으로 전체 운전비용을 약 30%정도 줄일 수 있었다.

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영양물질 주입에 의한 메탄 발효 주정폐액의 효율증진에 관한 연구 (A study on Enhanced Efficiencies of Methane Fermented Alcohol Wastewater Treatment by Supplement of Nutrients)

  • 안승구;이인학;진서형
    • 한국환경보건학회지
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    • 제23권3호
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    • pp.40-49
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    • 1997
  • In Korea, naked barley and tapioca are main raw materials for the production of fermentation ethyl alcohol, and one million drums bf 95% fermentation ethyl alcohol is produced per year by use of them. Stillage of alcoholic fermentation is mostly digested by methane fermentation process, and methane gas occured if methane fermentation process is recovered and mixed with fuel to decrease 25-30% for total fuel used in factories. In the anaerobic digestion process of naked barley stillage, supplement of nutrients is necessary to slove the problems caused by inhibitory materials contained if stillage and deficiency of nutrients. Therefore, the objective of this study was to examine why the anaerobic digesters using the naked barley distillery wastewater have shown the poor digestability frequently and how to control it. As the poor digestion was supposed to be occurred by the lack of iron as trace nutrient, the experiments were carried out to find out the optimum dosage and the way of addition of iron and to assess the quantitative evaluation of the type of iron in digesters. Initially, bottle test as batch digesters and lab-scaled continuous flow digesters were used in order to determine the digestion characteristics with tapioca and naked barley distillery wastewater. According to the results of batch tests, the poor digestion was caused by volatile fatty acids and could be improved by adding of calcium. The activity of the methanogenic bacteria were increased remarkably when the iron was added to the digester in the form of mixture with substrates.

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지렁이 분변토와 주정슬러지 혼합 배양액을 이용한 Biofilter에서의 고농도 악취제거 (Removal of High Odor Concentration with Biofilter using Mixture of Earthworm Cast and Distillery Sludge)

  • 박종웅;장석조
    • 한국환경보건학회지
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    • 제40권2호
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    • pp.127-136
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    • 2014
  • Objectives: This study was conducted to investigate the removal of high odor concentration from swine wastewater treatment facility by full scale biofilter using liquid with deodorant mixed with earthworm cast and distillery sludge. Methods: The supply of the culture liquid to the microorganism on the media in the biofilter increases the activity and growth of biomass. The experimental equipment was biofilter tower with treatment capacity of 90 m 3/min. The experimental conditions included gas flow of $60m^3/min$, retention time of 20 sec, and gas/liquid ratio of 67. Results: With changing season from winter to summer, the inlet odor concentration of ammonia increased from 2.5 ppm to 29 ppm, and of hydrogen sulfide from 21 ppm to 91 ppm, respectively. The odor treatment system with biofilter using the culture liquid was stable when the high loading rate increased and showed excellent removal grade with an average of 96.7% for ammonia, and an average of 93.7% for hydrogen sulfide. The pH and SCOD in the recirculating culture liquid near the bottom of the biofilter tower decreased with operation time, but its influence on the odor removal rate was negligible, because the organic matter (SCOD) was replaced by some culture liquid supplied 2-4 times per day. Conclusions: The biofilter using culture liquid could successfully remove high odor concentration which was generated from swine wastewater treatment facility.

이상 UASB 공정을 이용한 주정폐수의 혐기성소화 (Anaerobic Digestion of Distillery Wastewater in a Two-phase UASB System)

  • 신항식;배병욱;백병천
    • 대한토목학회논문집
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    • 제10권4호
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    • pp.185-192
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    • 1990
  • 본 연구에서는 주정폐액의 고율처리를 위하여 이상 UASB 공정을 시험하였다. 상분리는 반응조의 pH를 조절하므로써 가능하였다. 유입폐수의 SS 농도가 4.1g/l일 때 산형성조는 유기부하 16.5kg $COD/m^3.day$까지 운전이 가능하였고, 이때 산생성율은 3.9g HAc/l.day를 나타내었다. 메탄형성조는 유기부하 44kg $COD/m^3.day$까지 운전이 가능하였으며, 이때 COD 제거율은 80%이었고 비가스 생성율은 16.51/l.day이었다. 두 반응조에서 입상슬러지가 형성된 이후에는 알칼리도의 주입없이 메탄조유출수의 재순환으로 산형성조의 pH를 적절하게 유지할 수 있었다.

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