• Journal of Soil and Groundwater Environment
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• v.13 no.1
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• pp.24-31
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• 2008

Sulfate reducing bacteria (SRB) is universally distributed in the sediment, especially in marine environment. SRB reduce sulfate as electron acceptor to hydrogen sulfide in anaerobic condition. Hydrogen sulfide is reducing agent enhancing the reduction of the organic and inorganic compounds. With SRB, therefore, the degradability of organic contaminants is expected to be enhanced. Ferrous iron reduced from the ferric iron which is mainly present in sediment also renders chlorinated organic compounds to be reduced state. The objectives of this study are: 1) to investigate the reduction of TCE by hydrogen sulfide generated by tht growth of SRB, 2) to estimate the reduction of TCE by ferrous iron generated due to oxidation of hydrogen sulfide, and 3) to illuminate the interaction between SRB and ferrous iron. Mixed bacteria was cultivated from the sludge of the sewage treatment plant. Increasing hydrogen sulfide and decreasing sulfate confirmed the existence of SRB in mixed culture. Although hydrogen sulfide lonely could reduce TCE, the concentration of hydrogen sulfide produced by SRB was not sufficient to reduce TCE directly. With hematite as ferric iron, hydrogen sulfide produced by SRB was consumed to reduce ferric ion to ferrous ion and ferrous iron produced by hydrogen sulfide oxidation decreased the concentration of TCE. Tests with seawater confirmed that the activity of SRB was dependent on the carbon source concentration.

• Journal of the Korean Ceramic Society
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• v.36 no.2
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• pp.167-171
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• 1999

Titanium dioxide bodies sintered at 130$0^{\circ}C$ for 10 h under the oxygen flowing were reduced with hydrogen in 1200, 1250 and 130$0^{\circ}C$ for 4~20 h. Reduction kinetics were evaluated by measuring a weight loss between before and after reduction, and the thickness of reduced layer, respectively. The reduction followed the parabolic rate law, indicating that the rate-determining process is diffusion. From the Arrhenius plots, the apparent activation energies for the reduction were obtained as 210$\pm$10 kJ/mol.

• Journal of the Korean Chemical Society
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• v.17 no.4
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• pp.275-285
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• 1973

The addition of one mole of aluminum chloride to three moles of sodium borohydride in tetrahydrofuran gives a turbid solution with enormously more powerful reducing properties than those of sodium borohydride itself. The reducing properties of this reagent were tested with 49 organic compounds which have representative functional groups. Alcohols liberated hydrogen immediately but showed no sign of hydrogenolysis of alkoxy group. Aldehydes and ketones were reduced rapidly within one hr. Acyl derivatives were reduced moderately, however, carboxylic acids were reduced much more slowly. Esters, lactones and epoxides were reduced readily than sodium borohydride or borane. Tertiary amide was reduced slowly, however, primary amide consumed one hydride for hydrogen evolution but reduction was sluggish. Aromatic nitrile was reduced much more readily than aliphatic nitrile. Nitro compounds were inert to this reagent but azo and azoxy groups were slowly attacked. Oxime was reduced slowly but isocyanate was only partially reduced. Disulfide and sulfoxide were attacked slowly but sulfide and sulfone were inert. Olefin was hydroborated rapidly.

• Applied Chemistry for Engineering
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• v.5 no.1
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• pp.37-43
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• 1994

Mononitrotoluenes were reduced to aminotoluenes using porphyrin as a catalyst in the presence of several types of reductants including hydrogen sulfide and 1, 4-dithiothreitol(DTT). Intermediates and final products of porphyrin-catalyzed reduction of mononitrotoluenes were identified and a pathway for the reduction of the nitro group to the corresponding amino group was proposed. The optimum pH for the reduction was determined. The catalytic activity of the porphyrin was confirmed by UV/VIS absorption spectra and basic kinetics of porphyrin-catalyzed reduction were studied. Of several types of reductants tested, DTT sodium hydrosulfite, and hydrogen sulfide were seen to give significant reduction of nitrobodies. When hydrogen sulfide was used as a reductant hydrogen sulfide and nitrotoluenes were removed simultaneously.

• Transactions of the Korean hydrogen and new energy society
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• v.19 no.2
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• pp.132-138
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• 2008

금속산화물의 열화학싸이클에 의한 수소생산 소재중 안정성이 우수하고 물분해 수소생산능이 비교적 우수한 $NiFe_2O_4$를 합성하여 열화학수소생산공정 적용시 최적화의 조건에 대하여 검토하였다. 합성한 $NiFe_2O_4$는 격자상수가 $8.34\;{\AA}$이었고, 뫼스바우어에 의해 구조는 Ni이 페라이트 구조인 $AB_2O$의 B위치에 주로 위치하는, A 및 B의 상대적 흡수강도가 57.9:42.1인 역스피넬구조를 보이고 있다. 이러한 구조의 $NiFe_2O_4$의 열적환원은 $610^{\circ}C$부터 시작하여 $1200^{\circ}C$에 이르는 동안 약 1.1 wt%의 무게감소가 관찰된다. 물에 의한 산화과정에서 수소가 발생하게 되는데, $1200^{\circ}C$이하의 환원온도에서 가능한 수소생산량은 약 $0.45\;cm^3/g{\codt}cycle$ 이었다. 산화 환원의 반복과정에서 $NiFe_2O_4$의 XRD에 의한 구조변화는 관찰되지 않아 매우 안정한 구조를 갖는다는 것을 보여주었다. 수소생산을 위한 무게당 싸이클당 수소생산양은 산화 환원과정의 온도범위가 가장 중요하였고 물의 접촉시간은 중요한 요소가 되지 않았다. 열적 환원과정에서 많은 양의 수소생산성능을 보이기 위해서는 $1200^{\circ}C$이상의 고온을 필요로 하는 것을 보여주었다.

• Journal of Korean Society of Environmental Engineers
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• v.27 no.6
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• pp.635-641
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• 2005

Batch experiments were performed to evaluate the effect of sulfate reduction on methane production and reductive dechlorination, both compete for hydrogen with sulfate reduction. Dechlorination was inhibited by sulfate reduction at lower hydrogen concentration because their threshold values for hydrogen are similar (2 nM). Unlike methane production mainly inhibited transformation of cDCE to ethene, sulfate reduction inhibited the initial dechlorination step, PCE reduction into cDCE as well as cDCE dechlorination. The presence of sulfate eliminated methanogens as hydrogen competitor because of its high threshold value of 10 nM. When sulfate coexisted with PCE, dechlorination efficiency was not affected by the increase of seed concentration as both dechlorination and sulfate reduction were stimulated simultaneously by the increased seeding culture.

• Proceedings of the Korean Society of Soil and Groundwater Environment Conference
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• 2004.04a
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• pp.153-157
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• 2004

다양한 혐기성 조건에서 다환방향족탄화수소(PAHs)로 오염된 토양의 미생물 분해 연구를 수행하였다. 대표적인 다환방향족탄화수소인 phenanthrene과 fluorene을 토양과 물에 오염시켜서 약 100일 동안 저감정도를 관찰하였고, 실제 다환방향족탄화수소로 오염된 현장 토양을 이용 혐기성하에서 다환방향족탄화수소의 생분해 가능성을 확인하였다. 미생물 접종원은 혐기성 조건에서 다환방향족탄화수소에 노출시킨 슬러리가 사용되었다. 황산염 환원조건, 질산염 환원조건, 메탄생성조건 등의 다양한 혐기성 조건에서 실험을 수행한 결과, 메탄생성조건 > 질산염 환원조건 > 황산염 환원조건의 순서로 분해가 잘 일어났다. 또한 현장오염토양의 경우 34일간 처리 후 메탄생성조건에서 최대 72%의 분해율을 보였다.

• Resources Recycling
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• v.33 no.1
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• pp.15-21
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• 2024

The demand for electric vehicles powered by lithium-ion batteries is continuously increasing. Recovery of valuable metals from waste lithium-ion batteries will be necessary in the future. This research investigated the effect of reaction temperature on the lithium recovery ratio from hydrogen reduction followed by water leaching from lithium-ion battery NCM-based cathode materials. As the reaction temperature increased, the weight loss ratio observed after initiation increased rapidly owing to hydrogen reduction of NiO and CoO; at the same time, the H₂O amount generated increased. Above 602 ℃, the anode materials Ni and Co were reduced and existed in the metallic phases. As the hydrogen reduction temperature was increased, the Li recovery ratio also increased; at 704 ℃ and above, the Li recovery ratio reached a maximum of approximately 92%. Therefore, it is expected that Li can be selectively recovered by hydrogen reduction as a waste lithium-ion battery pretreatment, and the residue can be reprocessed to efficiently separate and recover valuable metals.

• Proceedings of the Korean Nuclear Society Conference
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• 1998.05a
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• pp.357-362
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• 1998

PWR 정지시 일차계통 수화학 제어의 주요대상은 계통표면에 침적된 부식생성물의 주성분인 비화학양론적 니켈(코발트)페라이트로서, 산성-환원 단계에서 용존수소에 의해 Ni$^{\circ}$ (또는 Co$^{\circ}$)로 환원되고 산성-산화 단계에서 용존산소에 의해 Ni$^{2+}$ (또는 CO$^{2+}$)로 산화되어 이온교환기에 의해 제거된다 본 연구에서는, 니켈 및 코발트 산화물의 25~300 $^{\circ}C$ 환원 또는 산화반응 시 표준자유에너지의 변화 및 용존수소 또는 용존산소의 요구농도를 계산하여, 원자로 정지시 일차계통수 용존 기체의 제어조건을 고찰하였다. 산성-환원 단계의 냉각재 온도인 300~82$^{\circ}C$ 범위에서 용존수소가 충분할 경우 열역학적으로 $^{58}$ Co(또는 $^{60}$Co)Fe$_2$O$_4$$\longrightarrow$Co의 역반응이 억제되므로서 노심외 계통부위 침적이 감소될 수 있기 때문에, 용존수소를 온도에 따라 요구농도 곡선 위로 약간 높게 유지하는 것보다 25~50 cc/kg-$H_2O$로 유지하는 방식이 바람직한 반면, 용존산소를 제공하는 과산화수소 농도가) 2.7 ppm일 때 NiFe$_2$O$_4$$\longrightarrow$Ni$_2$O$_4$(+$\alpha$-Fe$_2$O$_3$) 반응이 일어날 수 있기 때문에, 산성-산화 단계에서는 과산화수소의 냉각재 농도를 이보다 낮게 유지하는 것이 바람직하다.

• Journal of the Korean Crystal Growth and Crystal Technology
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• v.6 no.3
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• pp.415-423
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• 1996

Hydrogen reduction technique was used to form the nickel layer onto alumina powders in nickel sulfate solutions. The reduction rate and precipitation states of nickel ions were investigated at various experimental conditions such as hydrogen pressure, temperature, $PdCl_{2}$ addition, particle size, and so on. Uniformly nickel coated alumina composite powders were obtained at such condition as reduction temperature of $165^{\circ}C$, hydrogen pressure of 300 psi, and $PdCl_{2}$ amount of $2\;mg/\ell$.