化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2014年
9期
2339-2343
,共5页
陆敏%文艺%李树白%刘承先%程进
陸敏%文藝%李樹白%劉承先%程進
륙민%문예%리수백%류승선%정진
C5石油树脂%催化剂%催化%加氢
C5石油樹脂%催化劑%催化%加氫
C5석유수지%최화제%최화%가경
C5 petroleum resin%catalyst%catalysis%hydrogenation
通过对C5石油树脂的催化加氢,合成了浅色度C5石油树脂,制备并筛选了催化剂,采用固定床反应器对C5石油树脂进行了加氢工艺研究,采用BET、SEM和DTA-TG对催化剂进行了表征,用IR对C5石油树脂加氢前后的结构进行了分析。研究结果表明,Ni基多金属催化剂 C5JH-3在原料浓度为20%、温度为220~240℃、压力3.5MPa、空速0.5h-1、氢油比600∶1的条件下对C5石油树脂加氢,可制得软化点高的浅色度树脂。
通過對C5石油樹脂的催化加氫,閤成瞭淺色度C5石油樹脂,製備併篩選瞭催化劑,採用固定床反應器對C5石油樹脂進行瞭加氫工藝研究,採用BET、SEM和DTA-TG對催化劑進行瞭錶徵,用IR對C5石油樹脂加氫前後的結構進行瞭分析。研究結果錶明,Ni基多金屬催化劑 C5JH-3在原料濃度為20%、溫度為220~240℃、壓力3.5MPa、空速0.5h-1、氫油比600∶1的條件下對C5石油樹脂加氫,可製得軟化點高的淺色度樹脂。
통과대C5석유수지적최화가경,합성료천색도C5석유수지,제비병사선료최화제,채용고정상반응기대C5석유수지진행료가경공예연구,채용BET、SEM화DTA-TG대최화제진행료표정,용IR대C5석유수지가경전후적결구진행료분석。연구결과표명,Ni기다금속최화제 C5JH-3재원료농도위20%、온도위220~240℃、압력3.5MPa、공속0.5h-1、경유비600∶1적조건하대C5석유수지가경,가제득연화점고적천색도수지。
To obtain light-colored C5 petroleum resin , C5 petroleum resin was catalytically hydrogenated in a fixed-bed hydrogenation micro reactor. The C5 petroleum resin hydrogenation process was studied. Several hydrogenation catalysts were prepared and compared. The catalysts were characterized by nitrogen adsorption-desorption (BET),scanning electron microscopy (SEM) and differential thermal analyzer (DTA-TG). The petroleum resin and hydrogenated petroleum resin were characterized by FT-IR spectroscopy. The high softening point and light-colored C5 petroleum resin was obtained under the condition of Ni multi-metal catalyst C5JH-3,raw resin concentration of 20%, temperature of 220-240℃,pressure of 3.5MPa,space velocity of 0.5h-1,and hydrogen to oil ratio of 600∶1.