• Title/Summary/Keyword: 입상슬러지

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Characterization of Granular Fertilizer Produced by Fly Ash from a Sewage Sludge Incinerator (하수슬러지 소각 비산재를 이용한 입상비료 조립 및 특성분석)

  • Kim, Seong-beom;Lee, Wontae
    • Journal of Korean Society of Environmental Engineers
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    • v.38 no.10
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    • pp.574-579
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    • 2016
  • This study assessed feasibility of making granular fertilizer with fly ash from a sewage sludge incinerator in Korea. Composition, characteristics, strength, and heavy metal contents of the granular fertilizers were investigated. Due to its high contents of phosphorus, fly ash from a sewage sludge incinerator could be used to make fertilizers. Granulation rates (2-4 mm granules) over 80% could be achieved as the fly ash contents were 15% or less of the fertilizer. Leaching tests of the fertilizers, based upon the Korean Standard Methods for Solid Wastes, showed the concentrations of heavy metals less than the risk limits. However, contents analysis of the fertilizers, based upon the Korean Standard Methods for Soils, experienced higher levels of heavy metals than the risk limits as the fly ash content exceeded 7% of the fertilizer. Thus, the fly ash needs to be added less than 7% of the fertilizer if there is no pretreatment to remove heavy metals.

Ceramic Membrane Application for the Bayer Process of Aluminium hydroxide Production (수산화알루미늄 제조 Bayer 공정에서 Ceramic membrane 여과 실용화 공정 개발)

  • 김정학;이성오;구자경;남승하;이시철
    • Proceedings of the Membrane Society of Korea Conference
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    • 2003.11a
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    • pp.146-148
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    • 2003
  • Bayer 공정은 가성소다를 이용하여 보오크사이트로부터 수산화알루미늄을 추출하는 공정이다. 그러나 보오크사이트 추출 후 1차 침전공정에서 반응한 보오크사이트 잔사는 침전시킴으로써 깨끗한 공정액을 분리하는 데 이때 침전되지 못한 다량의 분산성 고형물이 공정액 중에 존재하게 되는데 이를 분산성 보오크사이트(레드머드) 미립자라하며 보통 80-100mg/$\ell$의 농도를 나타낸다. 그러므로 이를 제거하기 위해 다음 공정인 입상여과필터 공정을 사용하는데 이때 필터링 효율증대를 위해 보조제로써 다량의 소석회(Ca(OH)$_2$)를 투여하여 공정액 중의 고형물을 농도를 8-100mg/$\ell$에서 5mg/$\ell$로 낮추는 공정을 사용하고 있다. 특히 국내 수산화알루미능 제조회사일 KC(주)의 경우 소석회 사용량이 일 10톤, 년간 약 3,600톤을 사용함으로써 소석회의 사용량에 따라 같은 량의 슬러지가 발생되게 된다. 따라서 여과후 발생되는 슬러지의 처리비용 문제(연간 9천만원)와 소석회의 미립자에 의한 공정액의 2차 오염과 제품 품질 저하(quality claim) 및 소석회 사용량에 따른 연간 원료비(연간 3억원) 등의 상당한 문제점을 나타내고 있는 실정이다. 아울러 최근 고품위 수산화알루미늄의 공급 요구에 따라 여과시 정제기준이 점차 낮아져 이제는 1mg/$\ell$ 이하를 유지하여야 하는 근본적인 문제에 봉착해있는 실정이다. 그러므로 본 연구에서는 소석회를 사용하는 입상여과법을 대체하기 위한 신공정개발을 추진하였으며, 그동안 카트리지여과법 등의 다양한 실험 결과로부터 최근 필터 보조제를 첨가하지 않는 물리적 여과방법인 세라믹 막 여과법의 적용 가능성을 확인하고 친환경공정인 세라믹 막 여과 실용화 공정 기술을 개발하였다. 세라믹 막 여과 법은 여과 보조제를 사용하지 않으므로 2차적인 슬러지 발생등의 환경문제를 발생하지 않으며, 공정액에 첨가제를 투입하지 않으므로 순환형 친환경공정으로 각광받을 수 있다. 본 연구에서는 고온, 고농도의 NaOH 수용액의 처리에 적합한 막소재와 발생될 수 있는 제반 문제점 등을 파악하였고, 장기간의 실험을 거쳐 최적 투과 압력(Trans membrane pressue), 세정 조건 및 주기, 막재질에 있어서 보강하여야 할 Point, 최적 운전 조건들을 토출해 내었고, 향후 실제 Plant에 적용할 계획이다.

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Morphological Characteristics of Granular Sludge in dPAO SBR (dPAO SBR 입상슬러지의 형태학적 특성)

  • Yoo, Tae Uk;Lee, Hansaem;Yun, Geumhee;Yun, Zuwhan
    • Journal of Korean Society on Water Environment
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    • v.29 no.4
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    • pp.497-503
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    • 2013
  • The morphological characteristics of granules, which were generated in lab-scale sequencing batch reactor (SBR) for simultaneous nitrogen and phosphorus removal with denitrifying phosphorus accumulating organism (dPAO) were identified. Granular sludge was fully developed in the anaerobic-anoxic (An-Ax) SBR after 180 days of SBR operation. The average diameter of granular sludge was 2.2 mm and rod-type organisms dominated in the granules. In addition, about 1.0 mm of white precipitate was observed in the core of the granule, and the material was confirmed that it is very similar to hydroxyapatite $(HAP;\;Ca_5(PO_4)_3(OH))$ by X-ray diffraction) analysis.

A Comparative Study on the Morphological Characteristics of PAO and dPAO Granule (PAO와 dPAO 입상슬러지의 형태학적 특성에 대한 비교 고찰)

  • Yun, Geumhee;Yun, Zuwhan
    • Journal of Korean Society on Water Environment
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    • v.33 no.3
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    • pp.302-310
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    • 2017
  • The morphological characteristics of granules developing in anaerobic-anoxic (An-Ax) and anaerobic-aerobic (An-Ox) sequencing batch reactors (SBRs) were examined. The granules developed in the both SBRs after 200 days of laboratory operation. The average diameters of the granules were $2.2{\pm}1.7mm$ in the An-Ax SBR and $0.4{\pm}0.3mm$ in the An-Ox SBR. To determine the possible factors affecting morphology of granules a comparative analysis of various operating conditions from reference data indicated that the availability and type of electron acceptors is a key factor determining the granulation process and granular morphology.

The Methanogenic Toxicity of Wood Resin Constituents (메탄생성균에 대한 Wood resin 구성성분의 독성에 관한 연구)

  • 장봉기;허준무;손부순;박종안
    • Journal of environmental and Sanitary engineering
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    • v.12 no.3
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    • pp.139-147
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    • 1997
  • 펄프폐수 내에 존재하는 대표적인 수지 구성성분의 일종인 wood resin 화합물이 메탄생성균에 미치는 독성을 평가하기 위한 회분식 독성실험을 수행하였다. 수지는 극성용매로 추출가능한 몇몇 wood 구성성분의 혼합물로서 수지의 주요 구성성분은 긴 사슬 휘발성유기산, terpenes, resin acids, 리그난과 극성 페놀류들이다. 메탄생성균의 독성실험은 $30^{\circ}C$에서 표준회분식 실험방법을 채택하였고 식종물질로서는 입상슬러지를 사용하였다. 극성페놀의 한 종류인 4-hydroxystilbene가 가장 높은 독성을 나타내었으며, 50% 저해를 일으키는 농도는 $20mg/\ell$이었다. Resin acid와 휘발성 terpene 역시 메탄생성균에 독성을 나타내었으며, 50% 독성을 일으키는 농도는 $43{\;}~{\;}330mg/\ell$이었다. 반면에 triterpenes은 1,000 to $1,300{\;}mg/\ell$의 상대적으로 높은 농도에서도 메탄생성균에 독성을 일으키지 않았다. 따라서 wood resin의 구성성분이 몇몇 펄프폐수의 혐기성 처리에 있어서 독성을 일으키는 주요물질이었다.

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Shape and Formation of Aerobic Granulation in SBR (SBR에서 호기성 입상슬러지의 형성)

  • Yun, Zuwhan;Jang, Heeran;Han, Jonghun;Han, Hyejung
    • Journal of Korean Society on Water Environment
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    • v.20 no.5
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    • pp.534-538
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    • 2004
  • Granulation characteristics have been studied with an aerobic sequencing batch reactor(SBR). Organic loading of 2.46kg COD/$m^3$/day followed by 4.14kg COD/$m^3$/day had been applied to the lab-scale SBR with a very short settling time during the operating cycle. The granulation proceeded to the diameter range of 3 to 5 mm with MLSS concentration of 12,000mg/L at 45th days of operation while COD removal efficiency remained almost consistent after the granule formation. It has been noticed that aerobic granulation under the higher loading with a very short settling time seemed to be due to the microbial selection of better flocculating species.

Pore Structure and Adsorption Characteristics of Metals and Nutrient Salt of Activated Carbon Produced from Different Chemical Treatment (서로 다른 약품처리를 이용하여 제조한 활성탄의 세공구조 및 중금속과 영양염류 흡착특성)

  • Lee, Young-Dong;Kang, Hwa-Young
    • Journal of Korean Society of Environmental Engineers
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    • v.22 no.7
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    • pp.1319-1330
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    • 2000
  • Activated carbons prepared by chemical activation of organic waste sludges with $ZnCl_2$ and $K_2S$ have been studied in terms of their pore development and adsorptivity. Pore development of the carbons prepared from organic waste sludges was characterized by the nitrogen adsorption at 77K. The $ZnCl_2$-activated carbon produced by chemical activation with zinc chloride exhibited type I isotherm characteristics according to the BDDT classification, suggesting the presence of micropores formed by activation process. The isotherms of the commercial powdered activated carbon and $K_2S$-activated carbon reveal a hysteresis similar to that of type IV in BDDT classification, indicating the formation of mesopores. This result implies that the major pores of $K_2S$-activated carbon are composed of meso and micropores, and a macropores are minor. The adsorptive capacities of metal on the $K_2S$-activated carbon prepared from organic waste sludges were found to be superior to those on a commercial granular activated carbon. The Langmuir and Freundlich isotherms yield a fairly good fit to the adsorption data, indicating a monolayer adsorption of metals onto $K_2S$-activated carbon. The adsorptive capacity of the $K_2S$-activated carbon was superior to $ZnCl_2$-activated carbon for $PO_4$-P, and vice versa for $NO_3$-N. From the results of the studies reported here, it can be concluded that activated carbons with adsorptivity superior to commercial granular activated carbons can be produced from organic waste sludge using a two-step carbonization/activation procedure with zinc chloride or potassium sulfide as the activating agents.

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Investigation of Microbial Communities in the Anammox Reactor Seeded with Sewage Sludge and Anaerobic Granule (하수 슬러지와 혐기성 입상슬러지를 식종한 혐기성 암모니아 산화 반응기의 미생물 탐색)

  • Park, Kyung-Soon;Bae, Hyokwan;Chung, Yun-Chul;Park, Yong Keun;Jung, Jin-Young
    • Journal of Korean Society on Water Environment
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    • v.23 no.3
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    • pp.397-402
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    • 2007
  • Anammox reactor seeded with sewage sludge from RBC reactor and anaerobic granule from full-scale UASB reactor treating distillery wastewater was operated. Mixed granule and suspended sludge in the ammonium oxidizing process were taken and analyzed to investigate microbial community structure by molecular methods such as gene cloning and phylogenetic tree analysis after 250 days of continuous cultivation. The average nitrogen removal rate showed $0.9kg\;N/m^3-day$ after 250 days of continuous operation, then the maximum nitrogen removal rate showd $1.9kg\;N/m^3-day$ when $2.1kg\;N/m^3-day$ of nitrogen loading rate was applied. As results of gene cloning and phylogenetic tree analysis, Three kinds of phylum were found to be Proteobacteria, Acidobacteria and Planctomycetes (anammox bacteria) in mixed granule. Five kinds of phylum were found to be Proteobacteria, Chlorobi, Planctomycetes, Nitrospirae and Verrucomicrobia in suspended sludge. We found planctomycete KSU-1 and putative new anammox bacteria in the reactor. Microbial structure represented different consortia depending on the types of sludge in the anammox reactor.

Anaerobic Ammonium Oxidation(ANAMMOX) in a Granular Sludge Reactor and its Bio-molecular Characterization (입상 슬러지 반응조 내의 혐기성 암모늄 산화(ANAMMOX) 및 분자생태학적 특성 평가)

  • Han, Ji-Sun;Park, Hyun-A;Sung, Eun-Hae;Kim, Chang-Gyun;Yoon, Cho-Hee;Bae, Young-Shin
    • Journal of Korean Society of Environmental Engineers
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    • v.28 no.11
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    • pp.1213-1221
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    • 2006
  • In this study, granular sludge used in an anaerobic process treating brewery waste was inoculated in a laboratory scale of reactor to induce anaerobic ammonium oxidation(ANAMMOX). The reactor was operated with synthetic wastewater, which prepared at 1:1 ratio of $NH_4^+-N$ over $NO_2^--N$. Changes in nitrogen concentration, COD, alkalinity and gas production were analyzed. There are 3 phases of spanning in experimental period according to influent nitrogen concentration. In the Phase 1, each of the concentration of $NH_4^+-N$ and $NO_2^--N$ were increased from 1.91 $gN/m^3{\cdot}d$ to 14.29 $gN/m^3{\cdot}d$. Ammonium nitrogen loading(same as nitrite nitrogen) was 23.81 $gN/m^3{\cdot}d$ in the Phase 2 and 19.05 $gN/m^3{\cdot}d$ in the Phase 3, respectively $NO_2^--N$ has been removed up to 99% during whole period while the removal efficiency of $NH_4^+-N$ was significantly varied. In Phase 2, $NH_4^+-N$ was removed up to 75%. Microorganisms varied temporally through three phases were characterized by 16s rDNA analysis methods. ANAMMOX bacteria were dominantly found in phase 2 when the removal rate of $NO_2^--N$and $NH_4^+-N$ was the highest up to 99% and 75%, respectively. Due to erroneous exposed to air, the removal efficiency of $NH_4^+-N$ was unexpectedly lowered, but ANAMMOX bacteria still existed.

A Characteristics of Biogas Recovery and Biodegradability of Piggery Wastewater Using Granule of Two-Phase Anaerobic Process with UASB (UASB를 적용한 이상 혐기공정 granule에 의한 양돈폐수의 바이오가스 생성과 생분해 특성 평가)

  • Oh, SungMo;Bae, Yoon Sun;Park, Chul Hwi
    • Journal of Korean Society of Water and Wastewater
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    • v.21 no.3
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    • pp.315-322
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    • 2007
  • The purpose of this study was to investigate the biodegradability and performance of organic removal and methane production rate when treating piggery wastewater using a granule of two-phase anaerobic process applied UASB. BMP test was conducted as simple means to monitor relative biodegradability of substrate and to determine methane production of an organic material. The two-phase anaerobic process is consisted of a continuous flow stirred-tank reactor (CFSTR) for the acidification phase and an Upflow Anaerobic Sludge Blanket reactor (UASB) for the methanogenesis. The acidogenic reactor played key roles in reducing the periodically applied shock-loading and in the acidification of the influent organics. A stable maximum biogas production rate was 400mL. The methane contents ranged from 73 to 80% during the experimental period. It is known that most of the removed organic matter was converted to methane gas, and the produced biogas might be high quality for its subsequent use.