Abstract:
PURPOSE: Provided is a method for simultaneously extracting hydrocarbon using organic solvents during cultivation of microalgae, thereby extracting and recovering hydrocarbon in higher yield. CONSTITUTION: Hydrocarbon is characteristically produced by using a two-stage extractor consisting of a bubble column reactor and two-phase separating tank. The method for simultaneously extracting hydrocarbon using organic solvents during cultivation of microalgae comprises the steps of: supplying a culture medium from the bubble column reactor(1) to the two-phase separating tank(2) containing an organic solvent layer at a constant flow rate using a pump; recycling the culturing medium from the two-phase separating tank(2) to the bubble column reactor(1) through the organic solvent layer, wherein the hydrocarbon is extracted when passed through the organic solvent layer; and the organic solvent is alkane nonpolar solvent such as octane.
Abstract:
PURPOSE: A chromatography separation method using radially directed electric field is provided, which can control residence time of object material in the radial electric field according to the strength of electric field and relative polarity of an object material, a solvent and a packing material and can increase separation efficiency. Therefore the system can achieve high efficiency and high separation performance and also can be applied to chromatography of industrial scale. CONSTITUTION: The method comprises: i) applying voltage of more than 1V to chromatography column to form an electric field radially 1-10 minutes before charging sample; and ii) controlling residence time of the object material by controlling the strength of electric field. The equipment is characterized by a chromatography column (5), wherein an inside electrode (7) and an outside electrode (8) are installed inside and outside of the column respectively to charge electric field for separating an object material from a solvent and a packing material, the column having a channel with an inlet (11) and an outlet (12) for a coolant or heating media to flow.
Abstract:
PURPOSE: Provided is a process for producing chitosan oligosaccharide from polymer chitosan by hydrolysis using an edible organic acid useful for human bodies, which can be used for food additives and medical supplies. CONSTITUTION: The chitosan oligosaccharide is produced by dissolving the polymer chitosan in a water solution of the edible organic acid and performing the hydrolysis in an autoclave by applying microwave, wherein the edible organic acid is selected from the group consisting of tartaric acid, pyruvic acid, ascorbic acid, citric acid, lactic acid, propionic acid, acetic acid, and a mixture thereof and the concentration of the water solution of the organic acid is 3-8wt.%.
Abstract:
PURPOSE: A method for separating 2,6-dimethylnaphthalene with high purity is provided which solves the problem of loss of 2,6-dimethylnaphthalene and economical efficiency due to addition of the pre-treatment process and easily obtains the 2,6-dimethylnaphthalene with high purity. CONSTITUTION: A method comprises steps of: (i) selectively separating the mixture of dimethylnaphthalene isomer containing 2,6-dimethylnaphthalene from naphthalene mixture containing dimethylnaphthalene isomers by fractional distillation or recrystallization; and (ii) separating the 2,6-dimethylnaphthalene from the mixture of dimethylnaphthalene isomer containing 2,6-dimethylnaphthalene by pressure crystallization using solvent.
Abstract:
본 발명은 실리콘 나노선 및 피리딘을 사용하는 이산화탄소의 선택적 환원 방법에 관한 것이다. 본 발명의 여러 구현예에 따르면, 본 발명의 용액 에칭법으로 제조된 실리콘 나노선의 표면은 종래 실리콘 나노선보다 매우 거친 구조를 하고 있고, 이렇게 표면이 거친 실리콘 나노선 표면으로 태양광이 입사되면, 빛을 흡수할 수 있는 부분이 증가하고, 피리딘을 함께 사용함에 따라 이산화탄소 환원 반응에 경쟁적으로 일어나는 수소 생성과 같은 부반응이 많이 일어나는 문제점을 해결함과 동시에 이산화탄소를 선택적으로 환원 효율이 증가될 수 있을 뿐만 아니라, 종래 태양광에너지를 이용하여 이산화탄소를 연료로 전환하는 기술에 있어서, 높은 전압이 필요한 문제점을 해결할 수 있다.
Abstract:
PURPOSE: A treatment system of wastewater containing fluorine and method thereof is provided, in which fluorine ion is treated by supplying sufficient calcium ion together with air at pH of 7 to 7.5 efficiently by passing the wastewater through the lime packing towers(10,10') filled with cheap and safe natural lime instead of hydrated lime is filled. CONSTITUTION: In the treatment system comprising two lime filled packing towers(10,10') in which natural lime with a diameter of 2 to 2.8 mm is filled and two coagulating/settling towers(30,30'), the treatment method comprises the steps of feeding wastewater together with air to a first lime packing tower(10) upwardly; forming fluorine compound by allowing the incoming fluorine wastewater together with air to rest at the packing tower for 20 to 30 minutes; transferring the fluorine wastewater containing fluorine compound to the coagulating/settling tank(30); adding polymer coagulant to the fluorine wastewater followed by agitating at high or low speed; discharging the low fluorine content fluorine wastewater caused by formation of settlement a second lime packing tower(10').