• 상하수도학회지
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• 제28권1호
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• pp.135-142
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• 2014

The performance of inorganic sludge separation system is evaluated. Anaerobic digester effluent sludge is used for feed sludge of this system and hydrocyclone is used for inorganic sludge separation. For phosphorus removal and recovery $MgCl_2$ is pumped into MAP growth tank, a component of inorganic sludge separation system. Using this system inorganic sludge which contained less than 40 % of organic matter can be discharged stably and the maximum amount of separated inorganic sludge is 13.4 % of influent sludge based on dry solid. The amount of phosphorus recovered as MAP(as P) is 16.7 % to influent T-P.

• 한국분말재료학회지
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• 제21권2호
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• pp.142-146
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• 2014

Fundamental experiences have been studied for development of pre-treatment process of Sn by-products such as solders. Dry and wet separation/recovery processes were considered by the differences of physical properties. The by-products, which are analyzed by solder metal and oxides. The metal and oxide were simply separated by dry ball-milling process for 12 hours, after that recovery metal powder might be reusable as lead or lead-free solders. In terms of wet separation process, samples were dissolved in $HNO_3+H_2O_2$ and the precipitation were analyzed by $SnO_2$. Overall efficiency of recovery might be increasing via developing simple pre-treatment process.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 1998년도 공동 심포지엄 및 추계학술발표회
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• pp.97-105
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• 1998

The goal of this study is to investigate the potential application of triboelectrostatic separation process for removing unburned carbon from fly ash. The process utilizes the difference in electrical charging characteristics between the organic material (carbon) and the mineral matter (fly ash). In the present work, dry separation tests have been conducted on Samchunpo fly ash samples using a bench - scale analytic separator. The test variables studied include air rate, feed rate, electric field strength, particle size, charger material and length, etc. The best separation results were obtained at the air rate 501/min, feed rate 15 g/min and voltage 15 ㎸. The fly ash with carbon content below 1 % was obtained with over 65% recovery.

• 한국막학회:학술대회논문집
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• 한국막학회 1994년도 추계 총회 및 학술발표회
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• pp.32-33
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• 1994

Poly(vinyl alcohol)(PVA) membranes crosslinked with Glutaraldehyde (GA) were prepared for the separation of acetic acid-water mixtures. For the preparation of the crosslinked membranes, dry PVA films were immersed for 2 days at 40$\circ$C in reaction solutions which contain different content of GA solution(25% GA in water), aceton and a catalyst, HCl. IR spectroscopy was employed to characterize the crosslinking reaction between hydroxyl groups in PVA and aldehyde groups in GA. Swelling measurements of the crosslinked membranes were carried out in both water and acetic acid to investigate the crosslinking density and swelling behaviour of the membranes.

• Bulletin of the Korean Chemical Society
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• 제22권6호
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• pp.570-574
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• 2001

Magnesium isotope separation was investigated by chemical ion exchange with the 1-aza-12-crown-4 bonded Merrifield peptide resin using an elution chromatographic technique. The capacity of the novel azacrown ion exchanger was 1.0 meq/g dry resin. The heavier isotopes of magnesium were enriched in the resin phase, while the lighter isotopes were enriched in the solution phase. The single stage separation factor was determined according to the method of Glueckauf from the elution curve and isotopic assys. The separation factors of $^{24}Mg^{2+}$-$^{25}Mg^{2+}$, $^{24}Mg^{2+}$-$^{26}Mg^{2+}$, and $^{25}Mg^{2+}$-$^{26}Mg^{2+}$ were 1.008, 1.019, and 1.006, respectively.

• 멤브레인
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• 제6권3호
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• pp.117-126
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• 1996

Membrane-based gas separation systems are now widely accepted and employed as unit operation in industrial gas, chemical, and allied industries. Following their successful commercialization in the late seventies to recover hydrogen from ammonia purge gas streams, membrane-based systems have gained acceptance in a wide variety of applications. Numerous systems are in operation today to: recover hydrogen from other purge gas and hydrocarbon streams; adjust the $H_{2}/CO$ ratio in syngas; remove $CO_{2}$ from natural gas; recover helium; dry gas streams; and separate air. Lower cost, ease of operation, operational flexibility and portability are a few of the reasons membrane-based systems are chosen over absorption and cryogenic-based separations in certain applications.

• 한국광물학회지
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• 제27권4호
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• pp.311-320
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• 2014

슬래그를 매립한 토양을 대상으로 자기분리연구를 수행하였다. 토양세척을 거친 토양과 토양세척 전 토양을 대상으로 습식자기분리와 건식자기분리를 수행하여 분리된 부분과 분리되지 않은 부분의 중금속 농도를 측정하여 중금속의 농축효과를 측정하였다. 습식자기분리의 경우 토양세척 전 시료의 자력분리율이 상대적으로 높으며 토양세척 후 시료의 경우 약 40% 정도가 자기분리 되었다. 토양 : 물의 비가 농축효과에는 큰 영향을 미치지 못하며, Fe, Pb, Cu, Zn, Cd의 세척 전 토양과 세척 후 토양의 자기분리에 의한 평균 농축비는 3.2, 2.1, 12.1, 2.5, 1.5와 17.4, 7.0, 15.7, 9.6, 7.0으로 토양 세척을 거친 경우 자기분리에 의해 토양 세척 전 토양에 비해 더 큰 토양 부피 감량효과를 기대할 수 있다. 건식자기분리의 경우에도 자기분리에 의해 중금속의 농축효과를 얻을 수 있으나 자기분리에 의한 회수율이 너무 높은 경우 오염토 저감을 기대하기 어렵다. 철과 같은 강자성체를 포함하는 토양의 경우 자기분리에 의해 토양세척의 효과와 유사하게 오염토양의 양을 줄일 수 있고, 오염이 한쪽에 농축되는 결과를 얻을 수 있다.

• Journal of Mechanical Science and Technology
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• 제15권6호
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• pp.804-812
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• 2001

A triboelectrostatic separation system for removing unburned carbon from coal fly ash is designed and evaluated. Fly ash from a coal-fired power plant is used as an accepted additive in concrete where it adds strength, sulfate resistance and reduced cost, provided acceptable levels of unburned carbon are maintained. Unfortunately, unburned carbon in coal fly ash absorbs some of other additives and reduces the concrete strength. This paper describes to investigate dry triboelectrostatic process to separate unburned carbon from coal fly ash and utilize it into economically valuable products. The laboratory-scale triboelectrostatic separation system consists of a particle feeding system, a tribocharger, a separation chamber, and collection systems. Particles of unburned carbon and fly ash can be imparted positive and negative surface charges, respectively, with a copper tribocharger due to differences in the work function values of the particles and the tribocharger, and can be separated by passing them through an external electric field. Results showed that fly ash recovery was strongly dependent on the electric field strength and the particle size. 70wt% of fly ash containing 6.5wt% of carbon contents could be recovered at carbon contents below 3%. The triboelectrostatic separation system showed a potential to be an effective method for removing unburned carbon from coal fly ash.

• 대한원격탐사학회지
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• 제22권3호
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• pp.175-182
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• 2006

Because of the phenological variation of vegetation growth in temperate region, it is often difficult to accurately assess the surface conditions of agricultural croplands, grasslands, and disturbed forests by multi-spectral remote sensor data. In particular, the spectral similarity between soil and dry vegetation has been a primary problem to correctly appraise the surface conditions during the non-growing seasons in temperature region. This study analyzes the spectral characteristics of the mixture of dry vegetation and soil. The reflectance spectra were obtained from laboratory spectroradiometer measurement (GER-2600) and from EO-1 Hyperion image data. The reflectance spectra of several samples having different level of dry vegetation fractions show similar pattern from both lab measurement and hyperspectral image. Red-edge near 700nm and shortwave IR near 2,200nm are more sensitive to the fraction of dry vegetation. The use of hyperspectral data would allow us for better separation between bare soils and other surfaces covered by dry vegetation during the leaf-off season.

• 자원리싸이클링
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• 제25권1호
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• pp.40-47
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• 2016

니켈 산화광인 라테라이트광은 건식제련 원료인 사프로라이트광과 습식제련 원료인 리모나이트광으로 구성되어 있다. 사프로라이트광이 혼재된 리모나이트광을 습식제련용으로 사용할 경우 무기산 소모량이 증가할 뿐만 아니라 슬러지 발생량이 증가하여 공정비용을 증가시키는 단점이 발생한다. 이러한 이유로 니켈 리모나이트광은 Si+Mg함량 10% 이하, Fe 함량 40% 이상이어야 습식제련 원료로 사용하기 적합하다. 본 연구에서는 뉴칼레도니아산 니켈 라테라이트광을 대상으로 습식제련 원료인 리모나이트광을 분리선별하는 연구를 수행하였다. 뉴칼레도니아산 니켈라테라이트광의 입도에 따른 광물성분 및 화학성분 변화를 규명하여 분급에 의한 사프로라이트 및 리모나이트의 광물간 분리선별 가능성을 확인하였다. 뉴칼레도니아산 니켈 라테라이트 원광(함수율 23.0%) 및 니켈 라테라이트 건조광(함수율 9.1%)을 핀밀을 이용 해쇄한 후 건식분급한 결과, 니켈 라테라이트광을 함수율 9% 수준으로 건조할 경우 분급효율이 높아지는 것을 확인하였다.