Abstract:
A method for hydrolyzing cellulose is provided to suppress by-products, to be environment-friendly and to improve the yield while increasing the production rate of glucose. A method for hydrolyzing cellulose comprises (i) a step for pre-processing the cellulose by adding the ionic liquid in the cellulose; and (ii) a step for hydrolyzing the cellulose by adding a solid acid-catalyst to the pre-processed cellulose. The solid acid-catalyst is the zeolite.
Abstract:
The present invention relates to a method for manufacturing a nanocomposite active material for a lithium secondary battery comprising the steps of: producing a first cathode active material represented by Li2MnO3 by mixing a lithium compound and a manganese compound; producing a co-precipitated hydroxide represented by (Nia-Mnb-Coc)(OH)2 by mixing nickel sulfate, manganese sulfate, a solution mixed with cobalt sulfate, sodium hydroxide solution, and aqueous ammonia; producing a second cathode active material represented by LiMO2(M=Nia-Mnb-Coc) by mixing the co-precipitated hydroxide and a lithium compound; and mixing the first cathode active material and the second cathode active material. Electrochemical properties such as stability in the range of high voltage, electrode capacity and cycle lifetime can be improved by producing nanocomposite for a lithium secondary battery represented by the chemical formula below. [chemical formula] xLi2MnO3-(1-x)LiMO2.
Abstract:
이온성 액체와 산성용 이온 교환 수지를 사용하여 셀로비오스를 가수분해하는 방법이 개시된다. 상기 가수분해 방법은 셀로비오스의 가수분해 반응의 효율을 향상시켜 높은 수율의 글루코오스 생성이 가능하다. 이온성 액체, 이온 교환 수지, 셀로비오스, 가수분해, 글루코오스
Abstract:
PURPOSE: A method for hydrolysis of cellobiose using ionic liquid and acidic ion-exchange resin is provided to improve the efficiency of hydrolysis of cellobiose and produce glucose in high yield. CONSTITUTION: A hydrolysis method of cellobiose is hydrolysis using ionic liquid and acidic ion-exchange resin. The ion-exchange resin is cation exchange resin containing a sulfonic acid. The active site density of ion-exchange resin is 0.1 ~ 6 eq./kg. The ion-exchange resin is maintained over 140°C.