Polymer electrolyte membrane fuel cell (PEMFC) performance degrades when hydrogen sulfide (H2S) is present in the fuel hydrogen gas; this is referred to as H2S poisoning. This paper reveals H2S poisoning on PEMFC by measuring electrical performance of single cell FC under various operating conditions. The severity of H2S poisoning depended on H2S concentration under best operating conditions(65℃ of cell temperature and 100% of anode humidification). H2S adsorption occured on the surface of catalyst layer on MEA, but not on the gas diffusion layer(GDL) by analyzing SEM/EDX data. In addition, MEA poisoning by H2S was cumulative but reversible. After poisoning for less than 150 min, performance of PEMFC was recovered up to 80% by just inert nitrogen gas purging.

The purpose of this study is to estimate concentration and emission unit of ammonia and hydrogen sulfide released from domestic chicken buildings by field investigation. Mean concentrations of ammonia and hydrogen sulfide emitted from chicken buildings were 18.25(±4.78)ppm and 807.53(±526.17)ppb for caged layer house, 14.48(±4.13)ppm and 644.82(±312.48)ppb for broiler house, and 6.16(±2.02)ppm and 284.75(±232.08)ppb for layer house with manure belt, respectively. Mean emission coefficients of ammonia and hydrogen sulfide were 0.951(±0.131) g hen^-1h^-1 and 2.956(±0.968) mg hen^-1h^-1 based on head whereas they were 0.575(±0.082) g m^-2h^-1 and 12.44(±3.536) mg m^-2h^-1 based on time. In conclusion indoor concentration and emission coefficient of ammonia and hydrogen sulfide were highest in caged layer housed, followed by broiler house and layer house with manure belt.

Metal sulfide powders such as MnS, MoS2 and FeS are simply used to the machinery processing improvement agent and solid lubricant in powder metallurgy industrial. And then, metal sulfide powders have received relatively little attention from powder metallurgy. Recently, the portable machine is one of the important interfaces between human or human and electronic machine. With the increase of the intelligent activity, the social and industrial demands for information display device and power source are increasing. The transition metal sulfide materials (FeS, ZnS) have received considerable attention due to the large variety of its electric, optical and magnetic properties. Among the metal sulfide, FeS2 is appealing superior material for applications in Li-2nd battery because of high capacity. ZnS is also a famous phosphor material with various luminescence properties, such as photoluminescence (PL) and electroluminescence (EL). So generally used in the fields of display, sensors and laser. Metal sulfide materials, therefore, are provided for most widely application in all industries. In recent years, material researchers have become increasingly interested in studying with synthesis of metal sulfide.

The likelihood of failure for the thinning of high temperature sulfide and naphthenic acid corrosion, which affect to a risk of facilities, was analyzed through the risk based inspection using API-581 BRD. We found that the corrosion rate was increased with increasing temperature and total acid number(TAN). And maximum value of the technical module subfactor(TMSF) was not varied with operating condition, but the TMSF was sensitively changed at the range of low temperature, low flow rate, and high TAN. Also, the TMSF was increased as an used year and inspection effectiveness increased, but it was increased as thickness, inspection number, and over design decreased.

In this study, the ZnS composite powders for host material in phosphor was synthesized in situ by mechanical alloying. As the mechanical alloying time increases, particle size of ZnS decreases. ZnS powders of in a mean size was fabricated by mechanical alloying for 10h. The crystal structures of ZnS powders were investigated by X-ray diffraction and the photo-luminescence properties was evaluated with the optical spectra analyzer. The steady state condition of mechanically alloyed ZnS was obtained as a mean particle size of in 5h milling. The sphalerite and wurtize structures coexist in the ZnS mechanically alloyed for 5h. The ZnS powder mechanically alloyed for 10h grows to the sphalerite structure. And the strong emission peaks of ZnS are observed at 480 nm wave length at the powders of mechanically alloyed for 10h, but the sphalerite and wurtize structures in ZnS coexist and emission peaks are not appeared at the powders of mechanically alloyed for 10h.

Benthic organisms dwell in sediment-water interface that contains significant amount of organic and inorganic contaminants. Their feeding behavior is highly related with sediment itself and pore water in the sediments, especially in ease of deposit feeder

The effects of mechanical alloying conditions on the formation of Mn-sulfide powders were analyzed. Impeller rotating speed, lubricant coating and added amounts of process control agent(stearic acid) were selected as a process control factor. MnS compounds are synthesized in 3 hours by mechanical alloying at the alternative milling condition. Discontinuous rotating speed of 1200rpm for 4 minutes and 1000rpm for 1 minute shows more effects on the compound formation of MnS. After coating of lubricant on the wall, elementary Mn and sulfur were partially remained by mechanical alloying. The friction effects of the wall and grinding media on the powders are significantly important to form the compound of MnS.

In consideration that a high tensile strength and ion exchange capacity are maintained as the swℓing of membrane is controlled by the coagulation of PSf with the introduction of ion exchange groups and PPSS without the introduction of ion exchange groups, the block copolymer of PSf and PPSS were synthesized. The cation exchange membrane was prepared by sulfonation with CSA and casted. The synthesized block copolymer and cation exchange membrane were characterized by FT-IR and their thermal stability was confirmed by TGA. The optimum sulfonation could be accomplished at a mole ratio of BPSf to CSA 1:3. The best electrochemical properties obtained by the optimal condition were area resistance of 4.37 Ωㆍtextrmcm2, ion exchange capacity of 1.71 meq/g dry membrane, water content of 0.2941 g H2O/g dry membrane, and fixed ion concentration of 5.81 meq/g H2O. When GBL was used as an additive, area resistance was increased by 13.7 % and ion exchange capacity was increased by 14.6%. When the membrane was fabricated in a form of composite using non woven cloth as a support. the tensile strength of membrane could be improved, but the electrochemical characteristics were not influenced.

V2O5-TiO2 catalysts were prepared by various methods. V2O5-TiO2 were prepared by sol-gel method with different drying conditions (aerogel and xerogel), and V2O5 supported on TiO2 obtained by sol-gel method with precipitation-deposition method and impregnation method. The performance of the V2O5-TiO2 catalysts was investigated for the selective oxidation of hydrogen sulfide in the stream containing both ammonia and excess water. All the catalysts showed good dispersion of vanadium and they had high H2S conversion with no or little production of sulfur dioxide. The V2O5-TiO2 aerogel catalyst prepared by sol-gel method with drying under super critical condition had the highest surface area which led to better catalytic activity compared to those by other synthesis methods.

본 연구 목적은 페널티원소가 포함된 정광을 질산용액으로 마이크로웨이브 용출하여 Bi와 As를 효과적으로 용출하고자 하였다. 정광시료에 대한 페널티원소와 유용금속들의 용출특성을 마이크로웨이브 용출시간, 질산농도 및 정광 첨가량에 대하여 조사하였다. 그 결과 페널티원소인 Bi와 As의 용출률은 마이크로웨이브 용출시간이 증가할수록, 질산농도가 증가할수록 그리고 정광 첨가량이 감소할수록 증가하였다. 정광과 광석광물을 마이크로웨이브 가열하자, Bi가 90% 이상 제거되었고, 황비철석은 자류철석-적철석으로 상변환 되었다. 고체-잔류물에 대하여 XRD분석한 결과, 단체 황과 anglesite가 나타났다. 단체 황과 anglesite의 XRD peak는 1분에서보다 12분에서, 0.5 M보다 4 M에서 그리고 5 g보다 30 g에서 intensity가 더 증가하였고 예리해졌다. 이와 같은 결과는 용출효율이 증가할수록 더 많은 단체 황과 anglesite가 생성되기 때문인 것으로 사료된다. 정광을 마이크로웨이브 가열하면 Bi와 As가 대기 중으로 손실되지만, 질산용액으로 마이크로웨이브 용출하면 Bi와 같은 유용금속이 용출되어 회수될 수 있음을 확인하였다.

본 연구는 acid bake-water leaching system (AWS)를 이용하여 Au 정광으로부터 경제적이고 친환경적인 유용금속 용출을 위하여 황산염 용매제의 적용성을 파악하는 것이다. AWS 실험은 전기로를 이용하여 다양한 baking 온도(100℃~500℃)와 황산염 용매제(H2SO4, K2SO4, (NH4)2SO4, MgSO4, CaSO4) 조건에서 수행하였다. Baking 온도가 400℃까지 증가할수록 유용금속의 용출률은 증가하였다. 용출시간에 따른 AWS 실험결과, 최대 용출률 조건은 (NH4)2SO4 용매제이었다. 본 연구를 통하여 (NH4)2SO4 용 매제가 AWS를 이용한 유용금속 용출에 있어 효과적인 용매제로 사용가능함을 입증하였다.

지구온난화 문제와 유기성 폐기물의 처리문제는 해결이 시급한 환경문제이며, 바이오가스는 이러한 문제를 동시에 해결할 수 있는 장점으로 크게 주목받고 있다. 그러나 바이오가스 중에 함유된 황화수소나 암모니아는 발전설비의 부식 및 대기오염을 유발하기 때문에 전처리가 필수적이다. 기체상 오염물질의 처리를 위한 다양한 기술 중 수세정(scrubber)은 기액간의 접촉을 유도하여 액상으로 오염물질을 흡수 및 제거하는 기술로 널리 활용되고 있는 기술이다. 또한 황화수소나 암모니아는 물에 대한 용해성이 높기 때문에 수세정 공정을 활용하기 유리하다. 그러나 고농도의 황화수소나 암모니아를 효율적으로 처리하기 위해 가성소다 등의 약품을 세정액에 용해시켜 활용하는 것은 세정 후 약액의 2차 처리문제를 야기한다. 이에 본 연구에서는 이러한 문제점을 해결하기 위해 수세정공정에 전기화학적으로 생성된 free chlorine을 유입시켜 흡수된 황화수소 및 암모니아를 산화함으로써 물질전달률을 높일 수 있도록 하고자 하였다. 이를 위해서는 황화수소와 암모니아의 물질전달률의 평가가 필수적이며, 본 연구에서는 10mM의 NaCl이 용해된 수용액에 1,000 ppm의 황화수소와 암모니아가 4 L/min의 유량으로 단독으로 유입될 때와 동시에 유입될 때의 물질전달계수를 비교하였다. 수용액의 pH가 8일 때 황화수소 단독 물질전달계수(KLa-H2S)는 0.1214 min-1이고, 암모니아 단독 물질전달계수(KLa-NH3)는 9.9×10-5 min-1으로 산정되었다. 그러나 황화수소와 암모니아 각 1,000 ppm이 동시에 유입되었을 때 KLa-H2S는 0.2247 min-1, KLa-NH3는 1.6×10-4 min-1으로 물질전달속도가 상승하였다. 따라서 수세정 공정에서 황화수소와 암모니아의 동시유입이 제거율의 향상에 도움이 되는 것으로 나타났다. 또한, free chlorine에 의해 액상 황화수소와 암모니아가 제거된다면 추가적인 물질전달계수의 향상이 가능하다.