石油炼制与化工
石油煉製與化工
석유련제여화공
PETROLEUM PROCESSING AND PETROCHEMICALS
2014年
9期
47-51
,共5页
任永鹏%肖发新%赵迪%刘阳
任永鵬%肖髮新%趙迪%劉暘
임영붕%초발신%조적%류양
Pd/C 催化剂%还原温度%溶胶法%微观结构%精对苯二甲酸
Pd/C 催化劑%還原溫度%溶膠法%微觀結構%精對苯二甲痠
Pd/C 최화제%환원온도%용효법%미관결구%정대분이갑산
PdC catalyst%reduction temperature%sol-gel process%microstructure%purified tereph-thalic acid
采用钯溶胶法制备对苯二甲酸加氢精制用 Pd?C 催化剂,考察了还原温度对 Pd?C 催化剂活性的影响。通过 SEM、TEM、能谱、物理吸附、化学吸附等手段对 Pd?C 催化剂结构进行表征。结果表明:随着还原温度的升高,催化剂活性和分散度快速下降,当还原温度为10℃时,对羧基苯甲醛转化率接近100%,同时分散度也达到最高,所得催化剂 Pd 晶粒细小均匀,平均粒径为6.45 nm;30℃下制备的催化剂载体表面存在明显的团聚现象,Pd 晶粒平均粒径为15~20 nm,30℃下制备催化剂表面 Pd 含量约为10℃时的5倍;随着温度升高,聚氧乙烯基与水之间的氢键断裂,其增溶能力大幅下降,同时胶体中的 Pd 颗粒碰撞几率增加,造成胶体钯中 Pd 颗粒长大聚集,催化活性降低。
採用鈀溶膠法製備對苯二甲痠加氫精製用 Pd?C 催化劑,攷察瞭還原溫度對 Pd?C 催化劑活性的影響。通過 SEM、TEM、能譜、物理吸附、化學吸附等手段對 Pd?C 催化劑結構進行錶徵。結果錶明:隨著還原溫度的升高,催化劑活性和分散度快速下降,噹還原溫度為10℃時,對羧基苯甲醛轉化率接近100%,同時分散度也達到最高,所得催化劑 Pd 晶粒細小均勻,平均粒徑為6.45 nm;30℃下製備的催化劑載體錶麵存在明顯的糰聚現象,Pd 晶粒平均粒徑為15~20 nm,30℃下製備催化劑錶麵 Pd 含量約為10℃時的5倍;隨著溫度升高,聚氧乙烯基與水之間的氫鍵斷裂,其增溶能力大幅下降,同時膠體中的 Pd 顆粒踫撞幾率增加,造成膠體鈀中 Pd 顆粒長大聚集,催化活性降低。
채용파용효법제비대분이갑산가경정제용 Pd?C 최화제,고찰료환원온도대 Pd?C 최화제활성적영향。통과 SEM、TEM、능보、물리흡부、화학흡부등수단대 Pd?C 최화제결구진행표정。결과표명:수착환원온도적승고,최화제활성화분산도쾌속하강,당환원온도위10℃시,대최기분갑철전화솔접근100%,동시분산도야체도최고,소득최화제 Pd 정립세소균균,평균립경위6.45 nm;30℃하제비적최화제재체표면존재명현적단취현상,Pd 정립평균립경위15~20 nm,30℃하제비최화제표면 Pd 함량약위10℃시적5배;수착온도승고,취양을희기여수지간적경건단렬,기증용능력대폭하강,동시효체중적 Pd 과립팽당궤솔증가,조성효체파중 Pd 과립장대취집,최화활성강저。
A series of Pd?C catalysts for hydropurification of terephthalic acid were prepared using sol-gel process. The effect of reduction temperature on the microstructure and activity of the catalysts were investigated by means of SEM,TEM,EDS,physisorption,chemisorption and HPLC. The results show that the activity and dispersion of Pd sharply decreases with the increase of reduction temperature.The conversion ratio of 4-CBA is close to 100% at reduction temperature of 10 ℃ and the dispersion of Pd also reaches the highest. The Pd particles at this condition are fine and equally distributed with aver-age size of about 6.45 nm. However,a lot of larger particles with size of 15-20 nm gather at the sur-face at reduction temperature of 30 ℃. The amount of Pd on the catalyst surface reduced at 30 ℃ is about five times the amounts of Pd on the surface reduced at 10 ℃. Higher temperature generally causes the breaking of hydrogen bond between polyoxyethylene group and water,leading to a great reduction of solubilization capacity,which further results in the growth of Pd grain and the decrease of activity of Pd?C catalysts because of increased collision probability of Pd colloids.