功能材料
功能材料
공능재료
Journal of Functional Materials
2015年
22期
22133-22136,22140
,共5页
磷钨酸铝%Dawson 型%催化剂%酸中心%尼泊金丁酯
燐鎢痠鋁%Dawson 型%催化劑%痠中心%尼泊金丁酯
린오산려%Dawson 형%최화제%산중심%니박금정지
aluminium phosphotungstate%Dawson type%catalyst%acidic sites%butylparaben
采用复分解法制备出 Dawson 型磷钨酸铝(A1 H 3 P2 W18 O 62?n H 2 O)催化剂,通过 FT-IR、SEM、EDS、Py-IR 和 NH 3-TPD 对其进行了表征,并首次用于催化合成尼泊金丁酯.Py-IR 表征结果显示,A1 H 3 P2 W18 O 62?n H 2 O 同时具有 Br?nsted 酸中心和 Lewis酸中心.NH 3-TPD 测试结果表明 A1 H 3 P2 W18 O 62?n H 2 O 同时具有弱酸、强酸和超强酸中心,且以强酸中心为主.通过正交实验确定了合成尼泊金丁酯的优化工艺条件为催化剂用量4.9%(基于反应物质量),n (正丁醇)与 n (对羟基苯甲酸)=3∶1,反应时间3.0 h,反应温度120℃.在此条件下,尼泊金丁酯收率可达93.2%.与单纯 Dawson 型磷钨酸或浓硫酸催化效果相比,尼泊金丁酯收率得到提高.A1 H 3 P2 W18 O 62?n H 2 O 易于回收和重复使用,当重复使用5次后,尼泊金丁酯收率仍为73.1%.
採用複分解法製備齣 Dawson 型燐鎢痠鋁(A1 H 3 P2 W18 O 62?n H 2 O)催化劑,通過 FT-IR、SEM、EDS、Py-IR 和 NH 3-TPD 對其進行瞭錶徵,併首次用于催化閤成尼泊金丁酯.Py-IR 錶徵結果顯示,A1 H 3 P2 W18 O 62?n H 2 O 同時具有 Br?nsted 痠中心和 Lewis痠中心.NH 3-TPD 測試結果錶明 A1 H 3 P2 W18 O 62?n H 2 O 同時具有弱痠、彊痠和超彊痠中心,且以彊痠中心為主.通過正交實驗確定瞭閤成尼泊金丁酯的優化工藝條件為催化劑用量4.9%(基于反應物質量),n (正丁醇)與 n (對羥基苯甲痠)=3∶1,反應時間3.0 h,反應溫度120℃.在此條件下,尼泊金丁酯收率可達93.2%.與單純 Dawson 型燐鎢痠或濃硫痠催化效果相比,尼泊金丁酯收率得到提高.A1 H 3 P2 W18 O 62?n H 2 O 易于迴收和重複使用,噹重複使用5次後,尼泊金丁酯收率仍為73.1%.
채용복분해법제비출 Dawson 형린오산려(A1 H 3 P2 W18 O 62?n H 2 O)최화제,통과 FT-IR、SEM、EDS、Py-IR 화 NH 3-TPD 대기진행료표정,병수차용우최화합성니박금정지.Py-IR 표정결과현시,A1 H 3 P2 W18 O 62?n H 2 O 동시구유 Br?nsted 산중심화 Lewis산중심.NH 3-TPD 측시결과표명 A1 H 3 P2 W18 O 62?n H 2 O 동시구유약산、강산화초강산중심,차이강산중심위주.통과정교실험학정료합성니박금정지적우화공예조건위최화제용량4.9%(기우반응물질량),n (정정순)여 n (대간기분갑산)=3∶1,반응시간3.0 h,반응온도120℃.재차조건하,니박금정지수솔가체93.2%.여단순 Dawson 형린오산혹농류산최화효과상비,니박금정지수솔득도제고.A1 H 3 P2 W18 O 62?n H 2 O 역우회수화중복사용,당중복사용5차후,니박금정지수솔잉위73.1%.
Dawson type aluminium phosphotungstate was prepared by the precipitation method,and character-ized by FT-IR,SEM,EDS,Py-IR and NH 3-TPD.Then it was used in the preparation of butylparaben as cata-lyst for the first time.Results of Py-IR reveal that A1 H 3 P2 W1 8 O 62 has both Br?nsted and Lewis acid centers. NH 3-TPD results show that A1 H 3 P2 W1 8 O 62 has weakly acidic sites,strong acid sites and super acid sites,the major part of acid sites are strong acid site.The optimum esterification conditions determined by orthogonal ex-periments were:mass ratio of catalyst to reactants,4.9%;molar ratio of n-butyl alcohol to p-hydroxyl benzoic acid,3∶1;the reaction temperature,120 ℃;the reaction time,3.0 h.Under these conditions,the yield of bu-tylparaben was up to 93.2%,which is higher than those with Dawson type phosphotungstic acid or concentrated sulfuric acid as the catalyst.A1 H 3 P2 W1 8 O 62 can be easily recycled and reused,the yield of butylparaben remains up to 73.1% after 5 cycles.