• KSBB Journal
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• 제21권6호
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• pp.418-421
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• 2006

균질계 염기촉매를 이용한 바이오디젤을 생산하기 위한 전이에스테르화 반응의 원료유지 중에 유리지방산이 과다하게 존재하게 되면 유리지방산이 염기촉매와 결합하여 지방산 염 (비누)을 생성하여 상당량의 염기촉매를 소비하게 되어 촉매 투여량의 증가를 가져오게 된다. 또한 생성된 지방산 염 (비누)은 바이오디젤과 글리세롤의 상분리를 어렵게 하여 바이오디젤의 후처리 공정과 생산에 문제점을 야기시킨다. 따라서, 원료유지 내의 유리지방산은 균질계 염기촉매를 이용한 바이오디젤 생산공정에서는 원료중의 유리지방산은 반드시 제거되어야 한다. 본 연구에서는 원료유지에 고농도로 함유된 유리지방산을 제거하기 위하여 촉매로 ferric sulfate를 대상으로 전처리 공정을 수행한 결과 높은 유리지방산 (20%)을 함유하고 있는 모사 유지에서도 다른 이온교환수지에 비하여 우수한 성능을 얻었다. Ferric sulfate의 첨가량이 증가할수록, 메탄올의 첨가량이 증가할수록 유리지방산의 제거율이 증가하였다. 특히, ferric sulfate는 유지에 대해 낮은 용해성을 가지고 있어 반응 후 반응물로부터 쉽게 분리할 수 있고, ashing process를 통하여 재생이 가능하므로 원료유지의 전처리에 유용하게 적용할 수 있으리라 판단된다.

• 대한화학회지
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• 제59권4호
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• pp.280-283
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• 2015

Hydrated ferric sulfate can be used as an efficient and reusable catalyst for the synthesis of 2H-indazolo[2,1-b]phthalazine-trione derivatives via one-pot three-component condensation reaction of phthalhydrazide, aromatic aldehydes and cyclic-1,3-diketones in ethanol under reflux conditions.

• 공업화학
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• 제16권4호
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• pp.496-501
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• 2005

Iron계 금속 촉매의 존재 하에서 ABS의 열분해 거동을 TGA (Thermogravimetric Analysis)를 통해서 조사하였다. Iron계 금속 촉매(ferric nitrate nonahydrate, ammonium ferric sulfate dodecahydrate, iron sulfate hydrate, ammonium ferric oxalate, iron(II) acetate, iron(II) acetylacetonate 및 ferric chloride)는 ABS의 열분해 과정에서 화학반응을 야기하여, 질소분위기에서 촤(char)형성이 관찰되었으며, $600^{\circ}C$에서 3~23 wt%의 비휘발성 촤를 형성하였다. 이와 같은 질소분위기에서의 ABS의 촤 생성은 iron계 금속 촉매의 가교효과(crosslinking effect)로 추정된다. 한편, 공기분위기에서는 생성된 촤가 고온 산화반응에 의해서 열분해되었다.

• 한국염색가공학회지
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• 제17권6호
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• pp.51-59
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• 2005

To manufacture hightech easycare wool, there are several methods which use strong oxidising agent or the resin treatment, however, neither are environmentally friendly methods. Moreover it may deteriorate the handle. The aim of this study is to manufacture the hightech easycare wool using the modified Fenton method which can be formed by hydrogen peroxide and ferric sulfate and enzyme treatment. The method was pretreated by ferric sulfate on the wool surface and then the surface of wool scale was selectively removed by ferric ion catalyst. Subsequently the Enchiron which is one of the proteolytic enzymes was treated on the wool surface. The treated wool had the result of having optimum weight loss and excellent whiteness and good handle. Therefore implications of these results suggest that this method using the modified Fenton method and enzyme treatment may be one way of manufacturing the hightech easycare wool.

• 한국환경보건학회지
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• 제23권1호
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• pp.34-42
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• 1997

A laboratory experiments were performed to investigate the treatment of photographic processing wastewater by chemical oxidation and biological treatment system. The effect of reaction conditions such as hydrogen peroxide dosage, ferrous sulfate dosage and pH on the COD removal in Fenton oxidation were investigated. The optimal dosage of hydrogen peroxide was 2.58 M and 3.87 M for the developing and fixing process wastewater, respectively. The Fenton oxidation was most efficient in the pH range of 3-5 and the optimal condition for initial reaction pH was 5 for a developing process wastewater. With iron powder catalyst, the COD for a developing process wastewater was removed in lower pH than with ferrous sulfate catalyst. The removal efficiency of COD for refractory compounds such as Diethyleneglycol, Benzylalcohol, Hydroxylamine Sulfate, Ammonium Thiosulfate, Ammonium Ferric EDTA and Disodium EDTA in the photogaphic wastewater was found than 90% except Potassium Carbonate. When the photographic processing wastewater after pretreatment by Fenton oxidation was treated with batch activated sludge process, the addition of $KH_2PO_4$ as a phosphorous compound improved the removal efficiency of COD. During the continuous biological treatment of developing and fixing process wastewater after pretreatment by Fenton oxidation, the effluent COD concentration less than 100 mg/l was obtained at 0.425 and 0.25 kgCOD/m$^3$.d, respectively.