Abstract:
PURPOSE: A manufacturing method of a natural dye solution is provided to provide a natural dye solution capable of manufacturing various natural dye-sensitive solar batteries for requiring growth of plants. CONSTITUTION: A manufacturing method of a natural dye solution comprises a step of preparing a natural dye powder (400); a step of forming a natural dye solution by mixing the natural dye powder, pH controller, and solvent; and a step of forming a natural dye solution by mixing the natural dye powder, pH controller, and solvent. The natural dye solution has a wavelength selectivity for promoting or inhibiting growth of plant. The natural dye is Carthami Flos xanthophyll, lac color, alive side, red cabbage pigment, gardenia red, gardenia blue, rdenia Yellow, cacao, cochineal, henna, or monascus red. The manufacturing method is provided to control wavelength range by using the pH controller.
Abstract:
An activated carbon with ultra-high specific surface area which is prepared using corn, which has a specific surface area of 2500 m^2/g or more and an average pore size of about 2 nm, and in which a ratio of micropores to mesopores is controllable is provided, a method for preparing the activated carbon inexpensively and easily is provided, and various uses of the activated carbon including odor removal, water purification, natural gas adsorption, electric double layer supercapacitors, and catalyst carriers are provided. As a method for preparing an activated carbon with ultra-high specific surface area using corn grains, a method for preparing an activated carbon with a specific surface area of 2500 m^2/g or more using corn comprises the steps of: (A) drying and sorting raw material; (B) carbonizing the sorted raw material to a temperature of 500 to 1000 deg.C in an inert gas atmosphere; (C) mixing at least one activating agent selected from potassium hydroxide, sodium hydroxide, calcium carbonate, and zinc chloride with the carbide to activate the carbide, and controlling sizes of mesopores and micropores of the carbide while controlling content, activating time and activating temperature of the activating agent; and (D) cleaning and drying the size-controlled activated carbide. The step(B) is performed by carbonizing the raw material at 550 to 650 deg.C for 1 to 2 hours at a temperature rising rate of 5 deg.C/min. The step(C) is performed by activating the carbide at 700 to 1000 deg.C for 30 to 300 minutes using the activating agent to the carbide at a weight ratio of 1:1 to 5. The cleaning process in the step(D) is repeated until the cleaned carbide has a potential of hydrogen(pH) of 6 to 8.
Abstract:
염료감응 태양전지용 천연염료 용액 제조방법 및 이를 이용한 천연염료 감응 태양전지 제조방법을 제공한다. 염료감응 태양전지용 천연염료 용액 제조방법은 천연염료 분말을 준비하는 단계; 및 상기 천연염료 분말, pH 조절제 및 용매를 혼합하여 천연염료 용액을 형성하는 단계를 포함하고, 상기 천연염료 용액은 식물 생장의 촉진 또는 억제를 위한 파장 선택성을 갖는 것을 특징으로 하는 염료감응 태양전지용 천연염료 용액 제조방법을 포함한다. 따라서, 흡수파장대가 다른 천연염료 용액을 조합하여 제조된 파장선택용 칵테일 용액을 적용하여 식물의 생장에 필요한 파장대에 적합한 천연염료 감응 태양전지를 다양하게 제조할 수 있다.
Abstract:
An activated carbon with ultra-high specific surface area which is prepared using corn, which has a specific surface area of 2500 m^2/g or more and an average pore size of about 2 nm, and in which a ratio of micropores to mesopores is controllable is provided, a method for preparing the activated carbon inexpensively and easily is provided, and various uses of the activated carbon including odor removal, water purification, natural gas adsorption, electric double layer supercapacitors, and catalyst carriers are provided. As a method for preparing an activated carbon with ultra-high specific surface area using corn grains, a method for preparing an activated carbon with a specific surface area of 2500 m^2/g or more using corn comprises the steps of: (A) drying and sorting raw material; (B) carbonizing the sorted raw material to a temperature of 500 to 1000 deg.C in an inert gas atmosphere; (C) mixing at least one activating agent selected from potassium hydroxide, sodium hydroxide, calcium carbonate, and zinc chloride with the carbide to activate the carbide, and controlling sizes of mesopores and micropores of the carbide while controlling content, activating time and activating temperature of the activating agent; and (D) cleaning and drying the size-controlled activated carbide. The step(B) is performed by carbonizing the raw material at 550 to 650 deg.C for 1 to 2 hours at a temperature rising rate of 5 deg.C/min. The step(C) is performed by activating the carbide at 700 to 1000 deg.C for 30 to 300 minutes using the activating agent to the carbide at a weight ratio of 1:1 to 5. The cleaning process in the step(D) is repeated until the cleaned carbide has a potential of hydrogen(pH) of 6 to 8.