• 한국생물공학회:학술대회논문집
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• 2000.11a
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• pp.163-166
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• 2000

Hydrogen sulfide, ammonia and benzene which are generated from natural leather industry were simultaneously removed using biofilter including benzene degrading microbial consortia and sulfur oxidizer Thiobacillus sp.IW. The removal efficiency of benzene was maintained 90% in average for single and mixed gas treatment and that of ammonia was 99%, whereas at of hydrogen sulfide was relatively lower 85%.

• Proceedings of the Korean Society of Propulsion Engineers Conference
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• 2000.04a
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• pp.11-11
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• 2000

액체렘제트 엔진에서는 고온·고속의 공기가 공기흡입구로 유입되기 때문에 고성능 램제트 연소기의 설계를 위하여 실제 비행조건을 모사할 수 있는 고온 고속의 공기 발샐장치가 필요하다. 본 연구에서는 수소연소에 의해 Vitiated Air를 발생시키도록 설계된 Vitiated Air Heater(VAH)를 제작하였으며, VAH의 성능평가를 통하여 80∼120m/s 와 400∼800K 범위에서 손쉽게 속도와 온도의 조절이 가능하고 균일한 속도 및 온도분포로 대기공기와 같은 Vitiated Air를 얻을 수 있었다. 그리고 VAH을 연결하여 Dump형 연소기의 특성을 실험하였다. 액체 램제트 엔진에 있어서 공기흡입구가 하나인 Dump형 연소기에 주요변수로서 흡입공기의 온도와 공연비를 변화시키면서 연소기내의 화염형상을 관찰하고, 온도분포를 계측하였으며 Injection 위치에 따른 화염현상을 관찰하였다. 각 경우의 연소효율을 계산하여 실험범위에서의 최적 연소조건을 제시하였다.

• Proceedings of the Korean Institute of Information and Commucation Sciences Conference
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• 2003.10a
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• pp.953-956
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• 2003

천연광물질인 투어멀린은 물분자를 만나면 수소(H$^{+}$)와 수산기(OH$^{-}$)로 분해하여 친수기와 소수기를 구분하여 발생하며, H$^{+}$와 OH$^{-}$는 각각 $H_2O$와 결합하여 활성이 강한 hydronium ion(H$_3$O$^{+}$)과 계면활성 작용이 있는 hydroxyl ion(H$_3$O$_{2-}$ )을 생성한다. 물속에서 불안정한 상태로 존재하는 수산기는 hydroxyl (-)ion을 형성하여 약 알카리성(pH-7.4)을 띄고, 물의 클러스터(cluster)를 세분화하는 수질 개선 기능과 함께 살균, 항균 및 세균번식억제 효과를 갖는다. 그러므로 투어멀린 전기석의 물 분해 효과를 이용하여 이것을 일정 시간 동안 증류수에 침적시킨 뒤, 그 침적수를 대장균이 배양된 액에 드롭시켜 대장균의 변화를 조사하였다. 그 결과, 시간이 경과됨에 따라 대장균 수의 변화가 나타남을 확인하였고, 따라서 투어멀린 침적수의 대장균 증식억제 효과를 확인하였다.

• Korean Chemical Engineering Research
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• v.51 no.4
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• pp.455-459
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• 2013

The fuel processor for the portable fuel cell includes multi-step processes consisting of hydrogen generator, heat generator and several CO clean-up stages. One of requirements of the fuel processor for portable fuel cell system is a rapid start-up time. Especially, the warm-up time for WGS reactor is crucial factors for total start-up time. In this paper, active heating protocol, which is the heating protocol of WGS reactor supplied by the oxidation of CO rich reformate in the initial stage, is used for a rapid start-up. The air stream fed to the inlet of WGS reactor rapidly oxidize the CO rich reformate in the WGS reactor. Therefore, CO concentration in reformate quickly stabilized at the desired concentration without CO surges.

• Journal of the Korean Society of Propulsion Engineers
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• v.3 no.1
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• pp.86-94
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• 1999

Measured shock wave effects were investigated by changing shock strength and position with particular emphasis on the stability limits of hydrogen-air jet flames. For this purpose, a supersonic nonpremixed, jet-like flame was stabilized along the axis of a Mach 2.5 wind tunnel, and wedges were mounted on the sidewall in order to interact oblique shock waves with the flame. This experiment was the first reacting flow experiment interacting with shock waves. Schilieren visualization pictures, wall static pressures, and flame stability limits were measured and compared to corresponding flames without shock-flame interaction. Substantial improvements in the flame stability limits were achieved by properly interacting the shock waves with the flameholding recirculation zone. The reason for the significant improvement in flame stability limits is believed to be the adverse pressure gradient caused by the shock, which can elongate the recirculation zone.

• Korean Chemical Engineering Research
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• v.48 no.3
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• pp.382-390
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• 2010

In this research hydrogen sulfide, ammonia and toluene were designated as the representative source of malodor and VOC, respectively, frequently generated at the compost manufacturing factory and publicly owned facilities. The optimum operating condition to treat the waste air(2 L/min) containing malodor was constructed using photocatalytic reactor/biofilter process with humidifier composed of fluidized aerobic anf anoxic reactor. The ammonia(300 ppmv) of fed-waste air was removed by 22, 55 and 23% at the stage of photocatalytic reactor, humidifier and biofilter, respectively. The toluene(100 ppmv) of fed-waste air was removed by 20, 10 and 70% at the stage of photocatalytic reactor, humidifier and biofilter, respectively. Therefore the water-soluble ammonia and the water-insoluble toluene were treated mainly at the stage of humidifier and biofilter, respectively. In addition, hydrogen sulfide(10 ppmv) was almost treated at the stage of photocatalytic reactor and its negligible trace was absorbed in humidifier so that it was not detected before biofilter process. The nitrate concentration of the process water from anoxic reactor was found lower by 3 ppm than that from fluidized aerobic reactor. Besides, the dissolved ammonia-nitrogen concentration of the process water from humidifier remained at the high value of 1,500-2,000 ppm, which may be attributed to the existence of ammonium chloride and other source of ammonium nitrogen.

• Clean Technology
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• v.17 no.1
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• pp.69-77
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• 2011

The intrinsic $CO_2$ separation and hydrogen production system is a novel concept using oxidation and reduction reactions of oxygen carrier for both $CO_2$ capture and high purity hydrogen production. The process consists of a fuel reactor (FR), a steam reactor (SR) and an air reactor (AR). The natural gas ($CH_4$) is oxidized to $CO_2$ and steam by the oxygen carrier in FR, whereas the steam is reduced to hydrogen by oxidation of the reduced oxygen carrier in SR. The oxygen carrier is fully oxidized by air in AR. In the present study, the chemical looping moving bed reactor having 200 L/h hydrogen production capacity is designed and the hydrodynamic properties were determined. Compared with other reactors, two moving bed reactors (FR, SR) were used to obtain high conversion and selectivity of the oxygen carrier. The desirable solid circulation rates are calculated to be in the range of $20{\sim}100kg/m^2s$ from the conceptual design. The solid circulation rate can be controlled by aeration in a loop-seal. To maintain the gas velocity in the moving beds (FR, SR) at the minimum fluidization velocity is found to be suitable for the stable operation. The solid holdup in moving beds decrease with increasing gas velocity and solid circulation rate.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1998.05a
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• pp.79-84
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• 1998

고압 분류층 가스화기는 탄소전환율을 높이기 위해 고온, 즉 Ash Slagging 조건보다 높은 온도에서 운전된다. 따라서 분류층 가스화기에서 생산되어 배출되는 Raw Syngas는 고온의 현열을 보유하고 있다. 고온의 반응과정으로 인하여 타르나 기타 중탄화수소가 생성되지 않으므로 발생열을 회수하기가 용이하며 가스정제 및 불순물 제거과정도 단순해진다. (중략)

• Proceedings of the Korean Institute of Industrial Safety Conference
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• 1998.05a
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• pp.125-128
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• 1998

최근 많은 문제가 되고 있는 피혁공장, 유지공장, 슬러지처리장 등에서 발생하는 악취물질은 크게 산성 악취와 염기성 악취로 나눌 수 있으며, 대표적인 산성악취에는 메틸머켑탄, 황화수소가 있고, 염기성 악취는 암모니아, 트리메틸아민이 있다. 이들 악취물질들은 ACF의 표면을 화학약품으로 처리, 표면을 개질하여 관능기를 부여하고, 또한 화학물질을 첨착시켜 특정악취물질에 대한 제거효율을 증가시킬 수 있다. (중략)

• Journal of the Korea Academia-Industrial cooperation Society
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• v.4 no.3
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• pp.236-241
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• 2003

산업체 발생 VOC를 효과적으로 처리하는 Biofilter 시스템을 고안하였다. 재질과 다공성이 다른 3기의 시스템으로부터 황화수소, 벤젠, 톨루엔, 크실렌의 단일성분과 복합성분계의 성능을 고찰하였다 저 pH Biofilter(pH 2-3)의 장기운전이 가능하였고 벤젠의 경우 경쟁적 저해를 나타내었으나 일정기간의 순응 이후 혼합처리시 양호한 처리능력을 보여주었다.