Abstract:
PURPOSE: A coke oven gas increasing method using oxidant is provided to increase coke oven gas under the condition of minimizing the input of additional heat energy, thereby using the increased oven gas as a reductant or a heating source needed during an oven gas iron-making process or converting the increased oven gas into hydrogen. CONSTITUTION: A coke oven gas increasing method using oxidant comprises the following steps: providing oxidant including carbon dioxide and water to a carbonizing chamber (10) within a coke oven; and obtaining carbon monoxide and hydrogen by reacting carbon compounds or hydrogen inside the gas way of the carbonizing chamber with the use of the heat within the coke oven.
Abstract:
PURPOSE: An apparatus and a method for slag dry granulation are provided to improve the recovery rate of heat energy from high-temperature slag produced during the granulation of molten slag. CONSTITUTION: An apparatus for slag dry granulation comprises a main body(10), a slag collision rotator(50), and a circulating cooling gas flow forming unit(70). The slag collision rotator is installed in the main body in order to provide the collision and scattering of molten slag(30). The circulating cooling gas flow forming unit provides the main body with circulating cooling gas flow which passes through the main body and cools the molten slag. The main body includes a slag feed hopper(12) for putting in molten slag and a vent(14) for discharging high-temperature gas(G') heat-exchanged with slag particles(30').
Abstract:
PURPOSE: A method for predicting the concentration of reaction products in a carbon dioxide trapping process based on a regression analysis model without the omission of state variables measured through the carbon dioxide trapping process by implementing an online monitoring process in real time. CONSTITUTION: A state variable is measured through online by a carbon dioxide trapping process and is set as a varying variable(S100). The concentration of reaction products is obtained based on the varying variable through the carbon dioxide trapping process and is set online as a target variable(S200). A regression analysis model is modeled in order to predict the target variable(S300). The concentration of the reaction products is predicted through the regression analysis model based on the variation of the varying variable(S400).
Abstract:
PURPOSE: A chemical treatment method of carbon dioxide using industrial waste heat and a treatment apparatus are provided to reduce the energy to reduce/oxidize a reactant using the waste heat. CONSTITUTION: A chemical treatment method of carbon dioxide using industrial waste heat comprises the following steps: pre-treating coke oven gas before sending the coke oven gas to a heat exchanger; rapidly heating carbon dioxide using the industrial waste heat; exchanging the heat of the carbon dioxide with the coke oven gas in the heat exchanger; oxidizing the coke oven gas by reacting the high temperature coke oven gas with metal oxide; and reducing the carbon dioxide by reacting the carbon dioxide and the reduced metal oxide.
Abstract:
PURPOSE: Provided is a photocatalyst sol with high transparency and photoactivity, which is applicable to the fabrication of photocatalyst thin coatings on building interior, glass, aluminum chassis, lighting device and kitchenware. Also, a preparation method of the photocatalyst sol using titanium compounds is provided. CONSTITUTION: The method for preparing a photocatalyst sol includes the steps of mixing (a) titanium compounds selected from the group consisting of titanium isopropoxide, isopropoxide, TiCl4, and TiSO4, (b) organic solvents selected from ethanol, isopropanol, 2-butanol and ethyleneglycol, (c) surfactants selected from triton X-100, tween-20 and tween-80, (d) water and (e) catalysts, followed by heat treatment at 70 to 100 deg.C; mixing the resultant mixture solution with a binder solution; and agitating it at ambient temperature for 2 to 24 hrs to evaporate solvent, wherein the volatilization is continued until transparency of photocatalyst sol is over 90 % at 600 nm when one dip-coats the photocatalyst sol on slide glass. The photocatalyst sol exhibits greater photoactivity than 500 %/hr/% on methylene blue solution.