Abstract:
Provided is an apparatus for removing non-reacting coal in a coal gasifier. The apparatus for removing non-reacting coal in a coal gasifier according to an exemplary embodiment of the present invention can include a solid particle supply unit that supplies solid particles, which chemically react to coal, so that coal can be removed; and a pressurizing pump that is connected to an injection port so that the solid particles, which are supplied from the solid particle supply unit, can be injected through the injection port where a raw material for the coal gasifier is injected.
Abstract:
The present invention provides an algae cultivating method including a reactor provided with a carbon dioxide-containing flue gas supplying unit, a water supplying unit, and carbonic anhydrase, and producing carbonated water by making carbon dioxide-containing flue gas and water flowed into each of the supplying units react with the carbonic anhydrase; and an algae cultivating apparatus including an algae culture bath for cultivating algae using carbonated water. The method comprises the steps of: supplying carbon dioxide-containing flue gas, and water in the reactor including carbonic anhydrase; producing carbonated water by making the carbon dioxide react with water by carbonic anhydrase within the reactor; and cultivating algae using the produced carbonated water. The use of the algae cultivating apparatus and the algae cultivating method using the same can enhance carbon dioxide dissolution efficiency and algae productivity and reduce energy consumed in cultivating algae.
Abstract:
PURPOSE: A manufacturing method of ammonium bicarbonate is provided to manufacture ammonium bicarbonate with a low cost using gas-liquid reaction of ammonia solution and carbon dioxide generated from coal gasification process. CONSTITUTION: A manufacturing method of ammonium bicarbonate comprises the following steps. Ammonia generated from coal gasification process is collected to be ammonia solution. Carbon dioxide generated from coal gasification process is collected and ammonium bicarbonate slurry containing ammonium bicarbonate salt and water is generated using gas-liquid reaction with ammonia solution. The ammonium bicarbonate salt is collected by separating liquid from ammonium bicarbonate slurry. And ammonium bicarbonate is transformed into a solid state. The concentration of ammonia solution is 5-30%. Molality concentration of carbon dioxide molality/molality concentration of ammonia is 0.25-1 in the gas-liquid reaction of step. Ammonium bicarbonate manufacturing device includes reactor, solid-liquid separator, and dehydrator. [Reference numerals] (AA) Coal; (BB) Oxygen(O_2); (CC) Steam(H_2O); (DD) Gasifier; (EE) Oxygen facility; (FF) Synthetic gas; (GG) High concentration ammonia solution; (HH) Liquid reaction; (II) Gas refining; (JJ) Ammonium bicarbonate production apparatus; (KK) Ammonium bicarbonate slurry; (LL) Solid-liquid separator; (MM) Supernatant; (NN) Dehydrator; (OO) Dehydrated filtrate; (PP) Solid ammonium bicarbonate; (QQ) Waste heat returning power generation; (RR) Methane synthesis; (SS) Synthetic natural gas; (TT) Concentrated ammonia solution; (UU) Ammonia concentrator; (VV) Wastewater
Abstract:
PURPOSE: An environmental thermodynamic hydrate formation inhibitor is provided to thermodynamically suppress formation of a gas hydrate due to a reaction between gas and moisture and to be harmless to a human body and environment. CONSTITUTION: A hydrate formation inhibitor is an amino acid or a derivative thereof. The amino acid or the derivative thereof is one or more selected from L-proline, L-serine, glycine, L-alanine, and L-valine. A method for inhibiting formation of a hydrate comprises a step of injecting the amino acid or the derivative thereof into a moisture-containing gas up to a maximum solubility. [Reference numerals] (AA) Pressure(bar); (BB) Pure water(CSMGem); (CC) Pure water(example 1); (DD) Glycine 0.1 mole%; (EE) Glycine 0.5 mole%; (FF) Glycine 1.3 mole%; (GG) Glycine 2.2 mole%; (HH) Glycine 3.0 mole%; (II) Methanol 3.0 mole%; (JJ) Temperature(K)
Abstract:
본 광물 탄산화 방법은, 용출액이 포함된 용출반응기 내에 탄산화 원료 물질을 장입하여 칼슘 이온을 용출하는 제1 단계와, 상기 칼슘 이온이 용출된 상등액을 여과하여 탄산화 반응기에 유입하는 제2 단계와, 상기 탄산화 반응기 내에 탄산무수화효소 수용액 및 이산화탄소를 주입하여 광물 탄산화 반응을 촉진시킴으로써 탄산칼슘을 생성하는 제3 단계를 포함한다.
Abstract:
PURPOSE: Carbon dioxide collecting device and method using micro-bubbles are provided to collect carbon dioxide using a miniaturized device without a filler. CONSTITUTION: A carbon dioxide collecting method comprises the following steps: inserting mixed gas containing carbon dioxide into an absorptive tower(110); producing micro-bubbles using the mixed gas in a micro-bubble generator(130), floating the micro-bubbles to touch with absorption liquid inside the absorptive tower, and absorbing the carbon dioxide in the absorption liquid; transferring the absorption liquid containing the carbon dioxide to a regeneration tower(150); increasing the temperature of the absorption liquid in the regeneration tower for separating the carbon dioxide from the absorption liquid; and discharging the carbon dioxide to the upper side of the regeneration tower, and returning the absorption liquid to the absorptive tower.
Abstract:
PURPOSE: A method for predicting the concentration of a reaction product from a carbon dioxide collecting process and a collecting reactor are provided to optimize the collecting process by obtaining the optimal model of the collecting process from various models on the web. CONSTITUTION: A method for predicting the concentration of a reaction product from a carbon dioxide collecting process includes the following steps: a state variable measured through a carbon dioxide collecting process is set as a varying variable(S100); the concentration of a reaction product from the collecting process obtained using the varying variable is set as a target variable(S200); a model is generated to predict the target variable(S300); and the concentration of the reaction product according to the variation of the varying variable is predicted by the model(S400). The state variable is at least one selected from the concentration of carbon dioxide, the pH value, the temperature, and the electric conductivity of ammonia water containing absorbed carbon dioxide. The reaction product is one selected from a group including hydrogen ion, hydroxide ion, bicarbonate ion, carbonate ion, carbamate ion, ammonium bicarbonate, ammonium carbamate, sulfate ion, and nitrate ion. [Reference numerals] (AA) Start; (BB) End; (S100) Setting a state variable measured through a carbon dioxide collecting process through web as a varying variable; (S200) Setting the concentration of a reaction product from the carbon dioxide collecting process obtained using the varying variable as a target variable; (S300) Generating a model for predicting the target variable; (S400) Predicting the concentration of the reaction product according to the varying variable by the model
Abstract:
본 발명에 따른 금속의 부식측정방법은, 금속 분말을 준비하는 단계와, 금속 분말을 부식액에 침지하는 단계와, 광산란 장치를 이용하여 부식액에 의한 금속 분말의 크기 변화를 측정하는 단계를 포함하고, 시간에 따른 상기 금속 분말의 크기 변화를 측정하여 금속 분말의 부식율을 산출한다.
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).