Abstract:
본 발명은 유기황 화합물을 탈황시키는 신규의 크렙시엘라 옥시토카(Klebsiella oxytoca) 균주 및 그를 이용한 탈황방법에 관한 것이다. 좀 더 구체적으로, 본 발명은 석유와 석탄과 같은 화석연료내에 존재하는 황 함유의 유기타소 화합물로부터 황을 제거할 수 있는 신규의 미생물인 크렙시엘라 옥시토카 균주 및 그를 이용하여 화석연료내의 황 성분 또는 방향족 화합물을 제거하는 생물학적 방법에 관한 것이다. 본 발명의 분리균주는 고농도의 디벤조티오펜, 예를 들면 헥사데칸/디벤조티오펜 용해계나 유기황 농도가 높은 실제 연료유에 대해서도 효율적인 탈활효과를 나타내고, 종래의 탈황균주와는 달리, 균주생산의 탈황반응시 별도의 첨가물을 요구하지 않아 경제적이며, 바다 신속하게 탈황시킨다는 장점을 가지고 있다. 또한, 전기 분리균주는 유기황 화합물 뿐만 아니라, 기타 방향족 화합물들도 효과적으로 제거한다.
Abstract:
PURPOSE: A sulfuretted hydrogen removing device and a method for removing sulfuretted hydrogen are provided which are able to economically and effectively remove sulfuretted hydrogen contained in gas. CONSTITUTION: The device comprises: (i) an iron oxidation reacting tank which is able to cultivate iron oxidized microorganism; (ii) an absorbing tank which reacts the iron oxidized microorganism cultivated medium with gas containing sulfuretted hydrogen; (iii) a separator which is to separate a mixture solution of the cultivated medium/S0 slurry discharged from the absorbing tank; (iv) a bio-filter which is to remove the residual sulfuretted hydrogen contained in the discharge gas discharged from the absorbing tank; (v) a storage tank which is to store the cultivated medium discharged from the reacting tank, the absorbing tank and the separator; and (vi) a pump which is to transfer the cultivated medium from the iron oxidation reacting tank, absorbing tank, separator and the storage tank. The method comprises steps of: (i) producing an iron oxide solution by cultivating an iron oxidation microorganism in an iron oxidation reacting tank containing a fibrous microorganism fixation carrier, where the iron oxidation microorganism forms a biological film, and an iron oxidation microorganism cultivating medium; (ii) contacting the iron oxide solution with gas containing sulfuretted hydrogen to oxidize the sulfuretted hydrogen contained in the gas into a slurry of S0 and reduce the iron oxide solution into reduced iron solution; (iii) discharging the produced slurry of S0 and the reduced iron solution from the absorbing tank and separating them by using a separator; (iv) adjusting pH of the separated reduced iron solution into 1.7 to 2.3 by adding lime or calcium carbonate and then re-injecting the pH-adjusted reduced iron solution to the iron oxidation reacting tank to re-use it as a cultivation medium for producing an iron oxide solution; and (v) injecting discharge gas discharged from the absorbing tank into a bio-filter containing a carrier, where sulfated microorganisms are fixed on, to remove residual sulfuretted hydrogen contained in the gas.
Abstract:
PURPOSE: A method for recovering a biocatalyst and desulfurization oil from the emulsion generated during the biological petroleum desulfurization process is provided, to recover the desulfurized oil to the amount of 95 % or more without deterioration of the desulfurization performance. CONSTITUTION: A biocatalyst and desulfurization oil are recovered from the emulsion generated during the biological petroleum desulfurization process, by adding an alcohol to the three-phase emulsion of oil-biocatalyst-water and stirring the mixture; and separating the pretreated emulsion into three layers of an oil, a biocatalyst and water. Preferably the biocatalyst is Gordonia nitida CYKS 1 (KCTC0431BP). Also a biocatalyst and desulfurization diesel oil are recovered by adding ethanol to the three-phase emulsion of diesel oil-Gordonia nitida CYKS 1-water to the concentration of 1-4 % (v/v) and stirring the mixture; and separating the pretreated emulsion into three layers of a diesel oil, a Gordonia nitida CYKS 1 biocatalyst and water.
Abstract:
PURPOSE: A method for separating polyhydroxy-alkanoate from a microorganism is provided, thereby the installation cost and operating cost can be lowered, and polyhydroxy-alkanoate is simply separated in higher yield and purity, from a microorganism containing polyhydroxy-alkanoate in its body, with generating a little amount of liquid waste. CONSTITUTION: The method for separating polyhydroxy-alkanoate from a microorganism comprises the steps of: dissolving the cell components of a microorganism by adding SDS into the microorganism fermented culture containing polyhydroxy-alkanoate, and heating the solution with agitation to 50 to 150deg.C; recovering polyhydroxy-alkanoate from the treated solution; washing the recovered polyhydroxy-alkanoate with solvent; and drying the washed polyhydroxy-alkanoate, in which microorganism is selected from Alcaligenes latus, Alcaligenes eutrophus, Azotobacter vinelandii, Escherichia coli, Pseudomonas spp., and Methylotrophs, and SDS is added in an amount of 0.3 to 0.5g per 1g of dried microorganism containing polyhydroxy-alkanoate.
Abstract:
PURPOSE: A method for recovering a biocatalyst and desulfurization oil from the emulsion generated during the biological petroleum desulfurization process is provided, to recover the desulfurized oil to the amount of 95 % or more without deterioration of the desulfurization performance. CONSTITUTION: A biocatalyst and desulfurization oil are recovered from the emulsion generated during the biological petroleum desulfurization process, by adding an alcohol to the three-phase emulsion of oil-biocatalyst-water and stirring the mixture; and separating the pretreated emulsion into three layers of an oil, a biocatalyst and water. Preferably the biocatalyst is Gordonia nitida CYKS 1 (KCTC0431BP). Also a biocatalyst and desulfurization diesel oil are recovered by adding ethanol to the three-phase emulsion of diesel oil-Gordonia nitida CYKS 1-water to the concentration of 1-4 % (v/v) and stirring the mixture; and separating the pretreated emulsion into three layers of a diesel oil, a Gordonia nitida CYKS 1 biocatalyst and water.
Abstract:
본 발명은 유기황 화합물을 탈황시키는 신규의 크렙시엘라 옥시토카(Klebsiella oxytoca) 균주 및 그를 이용한 탈황방법에 관한 것이다. 좀 더 구체적으로, 본 발명은 석유와 석탄과 같은 화석연료내에 존재하는 황 함유의 유기탄소 화합물로부터 황을 제거할 수 있는 신규의 미생물인 크렙시엘라 옥시토카 균주 및 그를 이용하여 화석연료내의 황 성분 또는 방향족 화합물을 제거하는 생물학적 방법에 관한 것이다. 본 발명의 분리균주는 고농도의 디벤조티오펜, 예를 들면 헥사데칸/디벤조티오펜 용해계나 유기황 농도가 높은 실제 연료유에 대해서도 효율적인 탈황효과를 나타내고, 종래의 탈황균주와는 달리, 균주생산 및 탈황반응시 별도의 첨가물을 요구하지 않아 경제적이며, 보다 신속하게 탈황시킨다는 장점을 가지고 있다. 또한, 전기 분리균주는 유기황 화합물 뿐만 아닐, 기타 방향족 화합물들도 효과적으로 제거한다.