天然气化工
天然氣化工
천연기화공
NATURAL GAS CHEMICAL INDUSTRY
2014年
5期
27-30
,共4页
尹铎%马昱博%高志贤%李娜娜%吾满江·艾力
尹鐸%馬昱博%高誌賢%李娜娜%吾滿江·艾力
윤탁%마욱박%고지현%리나나%오만강·애력
双环戊二烯%氢甲酰化%三环癸烷不饱和单醛%三环癸烷二甲醛%催化剂%载体
雙環戊二烯%氫甲酰化%三環癸烷不飽和單醛%三環癸烷二甲醛%催化劑%載體
쌍배무이희%경갑선화%삼배계완불포화단철%삼배계완이갑철%최화제%재체
dicyclopentadiene%hydroformylation%monoformyltricyclo [5.2.1.02,6]dec-3-ene%diformyltricyclod-cane%catalyst%support
以粉体 SiO2、颗粒 SiO2、粉体 Al2O3、颗粒 Al2O3、MCM-41担载的0.1%Rh(以质量分数表示,下同)催化剂对双环戊二烯(DCPD)氢甲酰化合成三环癸烷不饱和单醛(MFTD)进行了对比研究,其中颗粒 SiO2和粉体 Al2O3具有最短的诱导期,仅有3min;以粉体 SiO2和粉体 Al2O3担载的0.1% Rh 为催化剂,可取得高达98.5%三环癸烷不饱和单醛的选择性;因此,较合适的高效合成三环癸烷不饱和单醛的载体为粉体二氧化硅和粉体氧化铝。以粉体 SiO2、颗粒 SiO2、粉体 Al2O3、颗粒 Al2O3、MCM-41担载的2% Rh 催化剂对双环戊二烯氢甲酰化合成三环癸烷二甲醛(DFTD)进行了对比研究,双环戊二烯的转化率都达到了100%,其中以粉体 SiO2和粉体 Al2O3担载的2% Rh 为催化剂,三环癸烷二甲醛的选择性达到了70%以上;在2h 的反应时间内,所有的催化剂催化合成三环癸烷二甲醛的反应进行的都比较快,但是仅有粉体 SiO2担载的2% Rh 催化剂在后续的反应时间里,展示了相对强劲的催化活性,在12h 的反应时间里,三环癸烷二甲醛的选择性可以达到91%,因此,较合适的高效合成三环癸烷二甲醛的载体为粉体 SiO2。
以粉體 SiO2、顆粒 SiO2、粉體 Al2O3、顆粒 Al2O3、MCM-41擔載的0.1%Rh(以質量分數錶示,下同)催化劑對雙環戊二烯(DCPD)氫甲酰化閤成三環癸烷不飽和單醛(MFTD)進行瞭對比研究,其中顆粒 SiO2和粉體 Al2O3具有最短的誘導期,僅有3min;以粉體 SiO2和粉體 Al2O3擔載的0.1% Rh 為催化劑,可取得高達98.5%三環癸烷不飽和單醛的選擇性;因此,較閤適的高效閤成三環癸烷不飽和單醛的載體為粉體二氧化硅和粉體氧化鋁。以粉體 SiO2、顆粒 SiO2、粉體 Al2O3、顆粒 Al2O3、MCM-41擔載的2% Rh 催化劑對雙環戊二烯氫甲酰化閤成三環癸烷二甲醛(DFTD)進行瞭對比研究,雙環戊二烯的轉化率都達到瞭100%,其中以粉體 SiO2和粉體 Al2O3擔載的2% Rh 為催化劑,三環癸烷二甲醛的選擇性達到瞭70%以上;在2h 的反應時間內,所有的催化劑催化閤成三環癸烷二甲醛的反應進行的都比較快,但是僅有粉體 SiO2擔載的2% Rh 催化劑在後續的反應時間裏,展示瞭相對彊勁的催化活性,在12h 的反應時間裏,三環癸烷二甲醛的選擇性可以達到91%,因此,較閤適的高效閤成三環癸烷二甲醛的載體為粉體 SiO2。
이분체 SiO2、과립 SiO2、분체 Al2O3、과립 Al2O3、MCM-41담재적0.1%Rh(이질량분수표시,하동)최화제대쌍배무이희(DCPD)경갑선화합성삼배계완불포화단철(MFTD)진행료대비연구,기중과립 SiO2화분체 Al2O3구유최단적유도기,부유3min;이분체 SiO2화분체 Al2O3담재적0.1% Rh 위최화제,가취득고체98.5%삼배계완불포화단철적선택성;인차,교합괄적고효합성삼배계완불포화단철적재체위분체이양화규화분체양화려。이분체 SiO2、과립 SiO2、분체 Al2O3、과립 Al2O3、MCM-41담재적2% Rh 최화제대쌍배무이희경갑선화합성삼배계완이갑철(DFTD)진행료대비연구,쌍배무이희적전화솔도체도료100%,기중이분체 SiO2화분체 Al2O3담재적2% Rh 위최화제,삼배계완이갑철적선택성체도료70%이상;재2h 적반응시간내,소유적최화제최화합성삼배계완이갑철적반응진행적도비교쾌,단시부유분체 SiO2담재적2% Rh 최화제재후속적반응시간리,전시료상대강경적최화활성,재12h 적반응시간리,삼배계완이갑철적선택성가이체도91%,인차,교합괄적고효합성삼배계완이갑철적재체위분체 SiO2。
A comparative study for synthesis of monoformyltricyclo [5.2.1.02,6]dec-3-ene (MFTD) by hydroformylation of dicyclopentadiene (DCPD) was carried out over the 0.1% Rh catalysts supported on the powder SiO2, the particle SiO2, the powder Al2O3, the particle Al2O3 and MCM-41, respectively. The results indicated that the powder SiO2 and the powder Al2O3 were the appropriate supports for MFTD synthesis, as the catalysts using them as supports had a short induction time of 3 minutes and high MFTD selectivity of up to 98.5% . A comparative study for synthesis of diformyltricyclodecane (DFTD) by hydroformylation of dicyclopentadiene was also carried out over the 2% Rh catalysts supported on the supports as used for above 0.1% Rh catalysts. The results showed that 100% DCPD conversion could be reached for all the catalysts, and DFTD selectivities of above 70% could be obtained for the catalysts supported on the powder SiO2 and the powder Al2O3. A fast reaction rate for DFTD synthesis within 2 hour reaction time were observed for all the catalysts, but only 2% Rh supported on the powder SiO2 showed a sustainable catalytic performance in all the reaction time and a DFTD selectivity of up to 91% could be achieved with it in 12 hour reaction. So, the powder SiO2 was the appropriate support for DFTD synthesis.