• Journal of the Korea Organic Resources Recycling Association
• /
• v.29 no.4
• /
• pp.99-106
• /
• 2021

The purpose of this study was to evaluate the performance of novel process with thermal hydrolysis and separation as pre-treatment of anaerobic digestion (AD). The dewatered sludge was pre-treated using THP, and then separated. The separated liquid used as substrate for AD and separated solid was returned on THP(Thermal Hydrolysis Process). The degree of disintegration (DD, based on COD) using only THP found 45.1-49.3%. The DD using THP+separation found 76.1-77.6%, which was higher than only THP. As result from dual-pool two-step model, the ratio of rapidly degradable substrate to total degradable substrate found 0.891-0.911 in separated liquid, which was higher than only THP. However, the rapidly degradable substrate reaction constant (kF) of only THP and THP+separation were similar. This results found that dewatered sludge was disintegrated by THP, and then rapidly degradable substrate of hydrolyzed sludge was sorted by separation.

• Proceedings of the Korea Water Resources Association Conference
• /
• 2016.05a
• /
• pp.591-591
• /
• 2016

최근에는 재이용을 위한 하 폐수의 처리 공정에 막을 이용한 기술적용이 증가되고 있는 추세이다(현 등, 2005). 막(membrane)을 이용한 수처리 공정은 원수에 상관없이 고도처리가 가능하며, 재이용수 이용 용도에 따른 수질제어가 가능할 뿐만 아니라 운용의 편리성 때문에 많은 각광을 받고 있다(박 등, 2004). 본 연구에서는 하수처리에 이용되는 분리막의 성능을 극대화하고, 분리막의 오염부하를 줄여주기 위하여 분리막 직전 전처리 시설로 부상방식의 고액분리장치를 개발하였다. 초고속 고액분리시스템은 기존의 응집부상공정을 응용한 기술로서 유기물의 응집시간을 최대 10초~2분 이내로 줄이는 기술을 바탕으로 타워형 모듈 형태로 개발하였다. 초고속 고액분리시스템과 분리막을 연계한 재이용수 수처리시스템의 성능 평가 및 현장적용을 위해 제주도 서부 하수 처리장에 일 $3,000m^3$ 규모의 Test-bed를 구축하였다. 구축된 하수재이용시스템의 처리 공정도는 "유입${\rightarrow}$고액분리시스템${\rightarrow}$분리막(UF, RO)${\rightarrow}$농경지 공급"으로 구성되어 있다. 먼저 하수처리장 방류수를 1차 유입조에 압송하면 전처리시설인 고액분리시스템을 통해 SS 등 입자성 물질이 처리되고, 다음 공정인 2차 처리공정(UF/RO)을 통과한 처리수는 인근지역의 농업용수로 공급되고 있다. 고액분리시스템은 ZT(Zeta Potential Tower) 모듈에서 유입수에 함유되어 있는 부유물질(SS), 유기물(질소, 인)을 응집제와 순간 반응시켜 응결, 응집, 부상방식으로 제거하는 공정이다. 고속 고액분리장치는 분리막 공정과 융 복합하여 다양한 유입수 성상에 따른 수처리를 가능하게 하여 재이용수 수질 향상뿐만 아니라 안정된 수자원 확보 측면에서 긍정적인 기술로 평가되었다.

• Journal of Animal Environmental Science
• /
• v.17 no.1
• /
• pp.33-38
• /
• 2011

Economic development involves increase in life expectancy as well as human health care. Consequently, demand for fish meal and fish oil is rapidly growing. In particular, Krill (Eupausia superba) oil product is in high demand due to its rich unsaturated-fatty acid, and thus stable supplies are necessary in the krill oil market. It is required for captured krills to be immediately frozen and stored during ship transport, since proteins of the krill are quickly denatured in natural temperature condition. However, the transportation cost has been sharply increased, which encourages researchers to involve in studies for development of efficient oil extraction process. In this study, a solid/liquid separation technique on boat for the krill oil was developed through triple separation tests using only a separator or using either brush or crusher prior to the separator. The separation tests revealed that the efficiency were 46.2, 60.2 and 60.4 % by the separator, combination with brush, and combination with crusher, respectively. In addition, it was found that byproduct, extracted cake, derived from the separation process could be used as a feed stuff. These results suggest that smashing using the brush or crusher prior to the separator is more efficient than using only the separator.

• Proceedings of the Korean Institute of Navigation and Port Research Conference
• /
• v.29 no.1
• /
• pp.305-309
• /
• 2005

This paper deals with an development of screen technology for marine waste disposal. The conception of inverse inclined screen is introduced. For optimal solid-liquid separation the vibration frequency, vibration angle and vibration method are inquired. And the efficiency of proposed technology and automatic apparatus is proved through the field test.

• Proceedings of the Korean Society for Agricultural Machinery Conference
• /
• 2017.04a
• /
• pp.102-102
• /
• 2017

제주산 감귤생산량은 51만톤(2016년)으로 수확기에 장마 등과 같은 환경적 요인에 의해 결점과의 비율이 24.9% 정도이다. 결점과로 통칭되는 비상품과는 일부 대기업의 쥬스공장에서 수매하는 량을 제외한 대부분은 자체 농장에서 폐기처분되고 있어 많은 감귤 비상품과 처리에 많은 문제점이 노출되어 오고있다. 성주군에서는 결점과 및 비상품과가 시장에 출하되는 것을 방지하기 위하여 자체 수매하여 액비, 발효퇴비, 사료화 가공 등에 많은 비용을 투자하고 있다. 따라서 본 연구는 당도가 15 Brix에 달하는 고당도 감귤 및 참외의 비상품과를 효과적으로 착즙하여 감귤 착즙액은 생산농자재로 환원하고, 참외 착즙액은 참외조청용 원료로 사용하는 기술을 개발하고자 한다. 착즙장치는 PLATE형 스크류, 테퍼 스크류 하우징, 파쇄된 과즙을 마지막 단계인 압입하는 고깔부 및 동력을 공급하는 구동부로 구성하였다. 개발한 고액분리 착즙장치의 외형은 $W1,000{\times}L2,000{\times}H1,070$이고 사용동력은 0,75kw, 1/30 감속모터를 사용하였다. 일반적인 착즙장치는 1단 분쇄와 동일 원통형의 스크류 압착으로 고액분리를 위한 착즙이 이루어지기 때문에 처리량이 150kg/hr에 불과하지만 개발한 고액분리장치는 2차 분쇄와 원통형과 원추형의 스크류 압착 후 고액분리망을 통과하도록 하여 500kg/hr 이상을 착즙이 가능하도록 개발하였다. 따라서 농산물의 고액분리를 통한 농산물의 가공을 위한 연속 착즙 장치는 2단 분쇄와 원통형 및 원추형 압착 미세망을 이용한 고액분리 착즙기는 기존 착즙기에 비하여 처리량이 3배 이상 증가되었다는 것을 알 수 있었다. 기존 감귤 착즙기의 수율은 60%정도이나 개발 착즙기의 착즙 수율은 66.5%로 나타나 본 연구에서 개발한 착즙기의 수율이 기존 착즙기의 수율보다 약간 높게 나타났다. 기존 착즙기는 원료(농산물의 종류)의 종류나 전처리에 제한이 있어 전용으로 사용하는데 비해 본 연구에서 개발한 고액분리 착즙기는 원료의 종류나 전처리 상태에 관계없이 사용 가능함을 확인하였다.

• Journal of the Korea Organic Resources Recycling Association
• /
• v.29 no.4
• /
• pp.107-114
• /
• 2021

This study applied with pre-treatment combined with thermal hydrolysis and seperation for disintegration of sludge. As results of particle size distribution D10, D50 and D90 of thermal hydrolyzed and centrifuged sludge was 8.6, 59.2 and 425.1 ㎛, which are lower than those of thermal hydrolyzed. The molecular weight distribution results showed that the thermal hydrolyzed sludge showed the highest proportion in the 10-100kDa range. But, Sludge, treated with combined pre-treatment, showed the highest proportion <1kDa range. Results of DOC and UVA₂₅₄ found that the organic matters of hydrolyzed sludge composed high molecular weight component above 10kDa. While, the organic matters of sludge, treated by combined pre-treatment, composed relarively low molecular weight below 1kDa. The specific methane yield of hydrolyzed and centrifuged sludge was higher 1.7 times than that of only hydrolyzed sludge.

• Journal of Animal Environmental Science
• /
• v.2 no.1
• /
• pp.79-86
• /
• 1996

Solid/Liquid(S/L) separation is crucial for biological treatment of animal wastewater. Liquid portion from S/L separation has less BOD-load and proper post-strip treatment can be obtained. Screen or declined sieve was normally used to separate the solid parts. For better separating efficiency a vibration and a cylindrical separator were constructed and tested. The results are summarized as follows; Solids removal efficiency and moisture content of separated solid were 15~26% and 85~88%, respectively for the vibration separator. for the cylindrical separator, solid removal efficiency and moisture content of solid were 16~39% and 86~89%, respectively. The greatest amount of drymatter was obtained when operating vibration separator with 10$^{\circ}$ inclination and 100% vibrating power. For the cylindrical separator maximum efficiency was obtained with 40 rpm and 19$^{\circ}$ inclination. The vibration and the cylindrical separator have shown 21% and 26% in BOD removal, respectively. These two types of separator were proved to be applicable methods for animal wastewater separation.

• Journal of the Korea Organic Resources Recycling Association
• /
• v.8 no.2
• /
• pp.60-70
• /
• 2000

The swine wastewater from slurry feedlot has been a social problem in Korea since the proper treatment is very difficult. Therefore, a practical study on the Solid-Liquid separation of swine wastewater from slurry feedlot was carried out as a pan of pretreatment for the successful biological treatment. The appropriate type of coagulant and optimum dosage were proposed for the most efficient Solid-Liquid separation and the best Solid-Liquid separation methods for different size of feedlot were determined through the tests with field-scaled Solid-Liquid separation equipment. The appropriate coagulant for the conditioning of dewatering property was E-851, which is a cationic polyelectrolyte made of polyacrylamide, and the optimum dosage was 0.24~0.6% of unit solids weight. Mesh Screen, Drum Screen, Cyclone Drum Filter, Screw Press, High-speed Screw Decanter, Low-speed Screw Decanter, and Dissolved Air Flotation Process had been investigated in this study. According to the results, the Screw Press was the best dewatering equipment for the small & medium size for feedlot and low-speed Screw Decanter was the best for the large size feedlot & public owned treatment facilities for the primary Solid-Liquid separation, and the most suitable secondary treatment process was DAF. On the other hand, reductions for the requirement of bulking agent and organic loading by Solid-Liquid separation process were 94.8% and 84.7%, respectively Therefore, the Solid-Liquid separation process must be required for the successful treatment of swine wastewater from slurry feedlot.

• Proceedings of the Membrane Society of Korea Conference
• /
• 1995.04a
• /
• pp.62-63
• /
• 1995

혐기성 소화는 고농도의 유기폐수를 최종적으로 메탄으로 전환하여 에너지원을 회수할 수 있는 효율적인 생물학적 폐수처리 공정 중의 하나이다. 그런데 이러한 혐기성 소화 공정에서 가장 큰 장애요인으로 작용하고 있는 요소 중의 하나가 매생물의 침강성 저하로 인한 고액분리의 문제이다. 이로인해 현재 고전적인 중력침강법, 부상법 대신에 분리막을 이용한 막결합형 혐기성 소화 공정이 대두되고 있으며 완전한 고액분리, 반응조내의 고농도 미생물 보유, 양질의 최종 유출수 획득 등 많은 장점들이 제시되고 있다. 그러나 이러한 장점에도 불구하고 시간에 따른 막오염 현상, 분리막 표면에서의 케이크층 형성 등으로 인한 막투과 유속 (flux)의 감소는 분리막의 응용에 있어 경제성을 저하시키는 주요한 부정적 요인으로 지적되고 있다. 그리고 막분리 성능은 분리막의 특성, 유체역학적 조건, 그리고 혐기성 소화 상태 등에 의해 영향을 받을 수 있다. 본 연구에서는 막결합형 혐기성 소화 공정의 십자흐름 (crossflow) 막분리 공정에서 유체역학적 조건 및 혐기성 소화조의 상태와 관련된 요인들이 어떻게 막투과도 및 배제율 등에 영향을 미치는 지 살펴보고자 한다.

• Journal of Environmental Health Sciences
• /
• v.28 no.5
• /
• pp.77-85
• /
• 2002

The objective of this study was to evaluate the performances of the ASBR under critical conditions of solid-liquid separation, caused by extremely high solids concentration, for wider application of the ASBR to various wastes. The ASBRs and completely-mixed daily-fed control runs were operated using a municipal mixed sludge at 35$^{\circ}C$ and 55$^{\circ}C$. Conversion of completely-mixed daily-fed reactor to sequencing batch mode and changes in HRT of all ASBRs were easily achieved without adverse effect, regardless of digestion temperature. Solids accumulation was remarkable in the ASBRs, and directly affected by settleable solids concentration of the feed sludge. Noticeable difference in solids-liquid separation was that flotation thickening occurred in the mesophilic ASBRs, while gravity thickening was a predominant solid-liquid separation process in the thermophilic ASBRS. Solids profiles at the end of thickening step dramatically changed at solid-liquid interface, and slight difference in solids concentrations was observed within thickened sludge bed. Organics removals based on subnatant or supernatant after thickening always exceeded 80% in all reactors. Thickened sludge volume and gas production of the ASBRs affected mutually. Gas production increased as thickened sludge accumulated, and continuous gas evolution during thickening could cause thickened sludge to expand or resuspend. Thickened sludge volume exceeding a predetermined withdrawal level resulted in loss of organic solids as well as biomass during withdrawal step, leading to decrease in gas production ind SRT. Such an adverse mutual effect was significant in gravity thickening, while it was not sensitive in flotation thickening. Changes in organic loading had no significant effect on organic removals and gas production after build-up of solids in the ASBRs.