Abstract:
본 발명은 페놀과 과산화수소를 반응시켜 파라벤조퀴논 및 카테콜을 제조하는데 사용되는 불균일 촉매로서, 상기 불균일 촉매는 바나듐 및 구리로 이루어진 군에서 선택된 1 종 이상의 금속 이온이 담지된 다공성 담체인, 파라벤조퀴논 및 카테콜 제조용 촉매에 관한 것이다. 또한, 본 발명은 상기 불균일 촉매를 사용하여 유기 용매 하에서 페놀과 과산화수소를 반응시켜, 총 생성물의 무게를 기준으로 90 무게% 이상의 파라벤조퀴논 및 카테콜을 제조하는 방법에 관한 것이다.
Abstract:
The present invention relates to: a production method of nickel-manganese complex hydroxide for a positive electrode active material of a lithium secondary battery which promotes the growth of precursor particles for producing the positive electrode active material compare to an existing coprecipitation method, and facilitates the control of the average particle diameter of the particles; and the positive electrode active material of a lithium secondary battery which uses the obtained nickel-manganese complex hydroxide for reducing the amount of fine powder in the precursor particles, improving the production yield of products, and increasing capacity and tap density.
Abstract:
본 발명은 고리형 탄화수소의 고리열림 반응공정 및 그 공정에 사용되는 촉매에 관한 것으로서, 금속성분과 산점을 동시에 함유한 이중기능성 촉매를 이용하여 납센 (고리형 탄화수소)의 선택적 고리열림 반응 (selective ring opening) 수행시 환원제 H 2 만을 단독으로 사용하는 경우와 비교하여 H 2 및 CO 2 를 동시에 사용하거나, CO 2 만을 사용하여도 H 2 만을 사용하는 경우와 같거나 혹은 더 우수한 전환율 및 선택도를 보이는 기술에 관한 것이다. 또한 본 발명에서 고리열림반응에 의한 생성물은 원료물질 보다 세탄가가 개선되어 디젤연료의 질을 증진하는 방법을 제공하는 것이다.
Abstract:
PURPOSE: A manufacturing method of a high-performance graphite-low temperature-cofired carbon composite negative electrode material is provided to manufacture a graphite-low temperature-cofired carbon composite negative electrode material including particles that are evenly distributed and increasing a battery initial efficiency and life characteristics of a battery. CONSTITUTION: A manufacturing method of a high-performance graphite-low temperature-cofired carbon composite negative electrode comprise the steps of: uniformly mixing graphite and a petrochemical byproduct to prepare a petrochemical byproduct-graphite composite; and carbonizing the composite in an inert atmosphere. The graphite is natural graphite or a cheap flake produced in a steel manufacturing process. The petrochemical byproduct is pyrolysis fuel oil, heavy crude oil, extra heavy crude oil, or a vacuum residue. A particle size and a surface area of the graphite-low temperature-cofired carbon composite negative electrode comprise are relatively in a range of 0.1 to 200 micron and 0.1 to 100 m^2/g.
Abstract:
PURPOSE: A nickel impregnated catalyst for selective cyclic opening reaction is provided to be used for improving process on cetane number of diesel fuel by lowering the content of ring compound component included in diesel oil light cycle oil(LCO). CONSTITUTION: A nickel impregnated catalyst for selective cyclic opening reaction is impregnated with nickel and one type or more of alkaline earth metal on the porous solid carrier. The sum of the impregnated nickel and one type or more of alkaline earth metal is 46-80 weight% based on the total weight.
Abstract:
PURPOSE: A technology for collecting and reforming improved oil sand is provided to inject a gas generating substance along with the application of a steam assisted gravity drainage technology, thereby lowering the viscosity of bitumen inside the oil sand, and producing a bitumen of which the maltene content is high. CONSTITUTION: A technology for collecting and reforming improved oil sand applying SAGD(Steam Assisted Gravity Drainage) includes: A steam and gas generating substance or steam, carbon dioxide gas, and a gas generating substance are simultaneously injected.; Temperature and pressure in the steam are transferred to an oil substance contained in the oil sand through the carbon dioxide gas and the gas generating substance.; The gas generating substance is decomposed at high temperature and high pressure so that at least one gas of ammonia, carbon monoxide or carbon dioxide can be generated.; The carbon dioxide gas, the gas generated from the gas generating substance, and bitumen interact with one another so that the viscosity of the bitumen can be lowered.; The carbon dioxide gas, the gas generated from the gas generating substance, and the bitumen react with one another at high temperature and high pressure. The gas generating substance has a chemical constitution of RR'N-CO-NRR', and simultaneously has a carbonyl group and an amine group. [Reference numerals] (AA) Weight(%); (BB) Room temperature
Abstract:
PURPOSE: A selective ring opening reaction process by carbon dioxide using a double functional heterogeneous catalyst is provided to use carbon dioxide or a compound having carbon dioxide and hydrogen as a reducing agent instead of hydrogen. CONSTITUTION: A selective ring opening reaction process by carbon dioxide comprises the following steps: supplying a ring type hydrocarbon and a reducing agent as supplying materials; transferring the supplied materials into a reactor(5), and reacting the mixture in the presence of a catalyst; and separating the resulting compounds from the effluent of the reaction. The catalyst is a heterogeneous catalyst containing an acid center and a metallic component.
Abstract:
PURPOSE: A method for manufacturing metal composite oxide is provided to promote the growth of precursor particles for manufacturing a positive electrode active material, to easily control an average particle diameter, and to increase a production yield. CONSTITUTION: A method for manufacturing metal composite oxide comprises the following steps: injecting a first metal salt solution with nickel and cobalt into a reactor in which distilled water is put; injecting a second metal salt solution having hydrogen ion concentration(pH) 6~12 into the reactor; and precipitating nickel composite hydroxide precursor particles by controlling pH of the whole metal salt solution in 11-13 while injecting NaOH solution and ammonia aqueous solution into the reactor.
Abstract:
PURPOSE: A catalyst for hydrocracking crude oil and a method for hydrocracking using the same are provided to reduce energy and processing cost with environment-friendly effects by performing a hydrocracking process in a low temperature and a low pressure conditions. CONSTITUTION: A catalyst for hydrocracking crude oil is the catalyst of a foam shape in which a reactive metal is dipped in a porous carrier. The catalyst for hydrocracking the crude oil has the total pore volume of 0.5 ~ 2.5 cc/g. The catalyst includes an air bubble surface area of 100 ~ 300 m^2/g. The thickness of pore wall of the catalyst is 5 ~ 100 nm. A pore diameter of the catalyst is 30 ~ 500 nm.