Abstract:
A method for manufacturing dimethoxymethane is provided to increase the production of dimethoxymethane due to the property of acid existing within a catalyst and to improve the oxidation reaction property in the methanol transformation reaction, compared with a unsupported catalyst by introducing a cation functional group to the mesopore carbon containing nitrogen and using a heteropolyacid catalyst. A method for manufacturing dimethoxymethane comprises a step for passing through the intermediate of dimethoxymethane by an acid-catalyzed reaction and a consecutive oxidation reaction of methanol or producing formaldehyde by the direct oxidation reaction of methanol; a step for preparing methoxymethanol by the acid catalytic reaction between the formaldehyde and methanol; a step for preparing dimethoxymethane by the acid catalytic reaction between methoxymethanol and methanol. In the chemical reaction, the heteropolyacid catalyst which can perform a Bi-functional catalyst of the acid catalytic reaction and oxidation reaction at the same time is used. The heteropolyacid catalyst is fixed to a mesopore carbon containing nitrogen having the average pore size of 2-50nm.
Abstract:
본 발명은 양이온 계면활성제를 주형물질로 사용하여 수열합성법(Hydrothermal Method)에 의해 제조된 중형기공 알루미나 담체에 담지된 니켈촉매, 그 제조방법 및 이를 이용하여 액화천연가스(LNG)의 수증기 개질반응에 의해 수소를 제조하는 방법에 관한 것이다. 본 발명은 촉매의 탄소침적 및 소결에 의한 비활성화에 대한 저항력을 증대시켜 장시간 동안 효율적이고 안정적인 운전이 가능하여 액화천연가스(LNG)의 수증기 개질반응에 의한 수소제조에 매우 효율적인 촉매를 제공한다. 중형기공 알루미나, 양이온 계면활성제, 니켈, 촉매, 수소가스, 액화천연가스(LNG), 수증기개질반응
Abstract:
PURPOSE: A nickel catalyst supported in a mesopore alumina carrier manufactured by a hydrothermal synthesis method using a cation surfactant is provided to offer stable catalyst activation, and offer excellent property for a long time. CONSTITUTION: A nickel catalyst supported in a mesopore alumina carrier is used for hydrogen manufacturing by steam reforming reaction of LNG. The mesopore alumina carrier is manufactured by a Hydrothermal Method with a cation surfactant used as a molding material. The nickel of 1-50 weight% is supported in the alumina carrier based on the total weight of the whole catalyst.