石油与天然气化工
石油與天然氣化工
석유여천연기화공
CHEMICAL ENGINEERING OF OIL AND GAS
2010年
2期
119-121,127
,共4页
伍锐东%马斐%唐善法%李国麟%刘忠运%陈琦%郑延成
伍銳東%馬斐%唐善法%李國麟%劉忠運%陳琦%鄭延成
오예동%마비%당선법%리국린%류충운%진기%정연성
轻石脑油%催化加氢%脱芳烃%操作参数
輕石腦油%催化加氫%脫芳烴%操作參數
경석뇌유%최화가경%탈방경%조작삼수
light naphtha%catalytic hydrogenation%dearomatization%operating parameters
实验评价了两种加氢催化剂的活性,并用优选出的催化剂对轻石脑油-催化重整抽余油进行了催化加氢脱芳烃实验.结果表明,QG-4和JSH两种催化剂均具有良好的加氢催化活性,但QG-4反应活性更高,脱芳效果更好,其在反应压力和反应温度分别为7MPa和450℃左右时可达到最佳活性;采用QG-4催化剂,对加氢操作参数进行优化,发现当反应压力为1.37MPa、反应温度为171℃、空速为2.0 h-1、氢油体积比为400时,可获得理想的脱芳效果及合理的成本投入,此时QG-4可将芳烃含量9.76×103mg/L降到1 mg/L以下,脱芳效果明显.
實驗評價瞭兩種加氫催化劑的活性,併用優選齣的催化劑對輕石腦油-催化重整抽餘油進行瞭催化加氫脫芳烴實驗.結果錶明,QG-4和JSH兩種催化劑均具有良好的加氫催化活性,但QG-4反應活性更高,脫芳效果更好,其在反應壓力和反應溫度分彆為7MPa和450℃左右時可達到最佳活性;採用QG-4催化劑,對加氫操作參數進行優化,髮現噹反應壓力為1.37MPa、反應溫度為171℃、空速為2.0 h-1、氫油體積比為400時,可穫得理想的脫芳效果及閤理的成本投入,此時QG-4可將芳烴含量9.76×103mg/L降到1 mg/L以下,脫芳效果明顯.
실험평개료량충가경최화제적활성,병용우선출적최화제대경석뇌유-최화중정추여유진행료최화가경탈방경실험.결과표명,QG-4화JSH량충최화제균구유량호적가경최화활성,단QG-4반응활성경고,탈방효과경호,기재반응압력화반응온도분별위7MPa화450℃좌우시가체도최가활성;채용QG-4최화제,대가경조작삼수진행우화,발현당반응압력위1.37MPa、반응온도위171℃、공속위2.0 h-1、경유체적비위400시,가획득이상적탈방효과급합리적성본투입,차시QG-4가장방경함량9.76×103mg/L강도1 mg/L이하,탈방효과명현.
The activity of two hydrogenation catalysts is evaluated, and catalytic hydrogenation dearomatization experiments of light naphtha-catalytic reforming raffinate oil are done. The results indicate that both catalysts of QG-4 and JSH have good reaction activity, and QG-4 has higher reaction activity and better dearomatization effect. Under the condition of 7MPa and 450℃, QG-4 has the maximum activity. The hydrogenation operating parameters are optimized using QG- 4 catalyst, the perfect dearomatization effect and reasonable cost could be acquired under the experiment condition when the reaction pressure is 1.37MPa, reaction temperature is 171℃, the space velocity is 2h-1, and the hydrogen oil ratio is 400. At that time, the QG-4 hydrogenation catalyst can decrease the aromatic content from 9.76×103mg/L to 1mg/L below.