化工技术与开发
化工技術與開髮
화공기술여개발
TECHNOLOGY & DVELOPMENT OF CHEMICAL INDUSTRY
2014年
2期
13-15,12
,共4页
张晓娟%邢春会%徐宏达%任君%李卫华
張曉娟%邢春會%徐宏達%任君%李衛華
장효연%형춘회%서굉체%임군%리위화
尼龙酸二甲酯%动力学%酯化反应%对甲苯磺酸
尼龍痠二甲酯%動力學%酯化反應%對甲苯磺痠
니룡산이갑지%동역학%지화반응%대갑분광산
nylon sour dimethyl ester%kinetics%esteriifcation reaction%toluene-p-sulfonic acid
以尼龙酸、甲醇为原料、对甲苯磺酸为催化剂,通过酯化反应合成尼龙酸二甲酯。根据反应过程中反应混合物酸值的变化跟踪反应,研究反应规律,建立了不分水条件下该反应体系的酯化反应动力学模型。计算结果表明,在55~65℃条件下合成尼龙酸二甲酯合成的正、逆反应对各组分均为1.3级反应,正、逆反应的表观活化能分别为6.291×104 J·mol-1、4.768×104 J·mol-1,指前因子分别为5.73×106、1.26×104。正、逆反应的速率常数均与催化剂浓度(用量)成0.3的指数关系。模型值与实验值相符,显示了该模型的正确性。
以尼龍痠、甲醇為原料、對甲苯磺痠為催化劑,通過酯化反應閤成尼龍痠二甲酯。根據反應過程中反應混閤物痠值的變化跟蹤反應,研究反應規律,建立瞭不分水條件下該反應體繫的酯化反應動力學模型。計算結果錶明,在55~65℃條件下閤成尼龍痠二甲酯閤成的正、逆反應對各組分均為1.3級反應,正、逆反應的錶觀活化能分彆為6.291×104 J·mol-1、4.768×104 J·mol-1,指前因子分彆為5.73×106、1.26×104。正、逆反應的速率常數均與催化劑濃度(用量)成0.3的指數關繫。模型值與實驗值相符,顯示瞭該模型的正確性。
이니룡산、갑순위원료、대갑분광산위최화제,통과지화반응합성니룡산이갑지。근거반응과정중반응혼합물산치적변화근종반응,연구반응규률,건립료불분수조건하해반응체계적지화반응동역학모형。계산결과표명,재55~65℃조건하합성니룡산이갑지합성적정、역반응대각조분균위1.3급반응,정、역반응적표관활화능분별위6.291×104 J·mol-1、4.768×104 J·mol-1,지전인자분별위5.73×106、1.26×104。정、역반응적속솔상수균여최화제농도(용량)성0.3적지수관계。모형치여실험치상부,현시료해모형적정학성。
The dimethyl adipate was synthesized through esterification reaction with nylon sour and methano using toluene-p-sulfonic acid as catalyst. Based on the acid value change of reaction mixture, the reaction was traced and the reaction rule was studied, and the kinetics model was established with the water no diversion. By kinetic calculation, it was obtained that the overall order of positive reaction and side reaction was 1.3 on 55~65℃, the apparent activation energy to positive reaction and side reaction was 62910J/mol and 47680J/mol, the frequency factor to positive reaction and side reaction was 5.73×106、1.26×104, the positive rate constant and side rate constant varied with the level of catalyst,they were both accord with exponential relationship of 0.3. The model values consistent with the experimental value, showed the correctness of the model.