摘要
研究了N,N-二甲基十二烷基酰胺的催化加氢反应,通过将Cu-C r催化剂与传统的加氢催化剂(如Cu-N i,Pd/C,Raney N i)进行对比,对加氢催化剂进行了筛选,实验结果表明,Cu-C r催化剂在N,N-二甲基十二烷基酰胺的催化加氢反应中具有较高的活性,当n(Cu)∶n(C r)=1∶1、还原温度200℃时,Cu-C r催化剂的活性最高。考察了反应温度、反应压力以及通入二甲胺气体对反应的影响,实验结果表明,二甲胺气体的通入有利于抑制副反应的进行;在反应温度230℃、反应压力3.0M Pa、反应后期通入二甲胺气体的条件下,N,N-二甲基十二烷基酰胺的转化率达99.5%,产物中N,N-二甲基十二烷基叔胺的质量分数达到85.3%,N,N-双十二烷基甲基叔胺的质量分数达到9.5%。
Hydrogenation of N, N-dimethyldodecylamide for preparations of N, N-dimethyldodecyl tertiary amine and N, N-didodecylmethyl tertiary amine was studied on different catalysts, namely Cu- Cr,Cu-Ni, Pd/C and Raney Ni. The two amines can be used as surfactants, Cu-Cr was the best catalyst under optimized conditions:n(CU) : n(Cr)1 : 1 and reduction temperature 200 ℃. Effects of reaction temperature, reaction pressure and addition of dimethylamine on hydrogenation were investigated. Addition of dimethylamine could effectively prohibit formation of byproduct lauryl alcohol. Under optimal conditions: reaction temperature 230℃, reaction pressure 3. 0 MPa, and addition of dimethylamine at later stage of reaction, conversion of N,N-dimethyldodecylamide could reach 99.5 %, and mass fractions of N,N-dimethyldodecyl tertiary amine and N, N-didodecylmethyl tertiary amine in products could reach 85.3 % and 9.5 %, respectively.
出处
《石油化工》
EI
CAS
CSCD
北大核心
2006年第6期557-560,共4页
Petrochemical Technology
基金
山西省自然科学基金项目(20031027)