石油与天然气化工
石油與天然氣化工
석유여천연기화공
Chemical Engineering of Oil and Gas
2015年
5期
55-59
,共5页
齐振东%鄢景森%魏民%王海彦
齊振東%鄢景森%魏民%王海彥
제진동%언경삼%위민%왕해언
SBA-15%磷化镍%喹啉%加氢脱氮
SBA-15%燐化鎳%喹啉%加氫脫氮
SBA-15%린화얼%규람%가경탈담
SBA-15%nickel phosphide%quinoline%hydrodenitrogenation
采用等体积浸渍法和H2原位还原法制备了Ni2 P/SBA‐15催化剂,分别考察了不同P/Ni比、还原温度、活性组分质量分数对加氢脱氮性能的影响。采用 X 射线衍射(XRD )、N2吸附脱附(BET )等技术,考察了SBA‐15分子筛及其催化剂形貌和织构性质,并以喹啉为模型化合物在微型固定床反应器上考察了不同温度对催化剂加氢脱氮(HDN )性能的影响。结果表明,当磷镍比为1,磷化镍质量分数为30%,还原温度为650℃时,其催化活性最好,在360℃、3 M Pa、氢油体积比500、液时空速2 h-1的反应条件下,喹啉的脱氮率可以达到85.6%。
採用等體積浸漬法和H2原位還原法製備瞭Ni2 P/SBA‐15催化劑,分彆攷察瞭不同P/Ni比、還原溫度、活性組分質量分數對加氫脫氮性能的影響。採用 X 射線衍射(XRD )、N2吸附脫附(BET )等技術,攷察瞭SBA‐15分子篩及其催化劑形貌和織構性質,併以喹啉為模型化閤物在微型固定床反應器上攷察瞭不同溫度對催化劑加氫脫氮(HDN )性能的影響。結果錶明,噹燐鎳比為1,燐化鎳質量分數為30%,還原溫度為650℃時,其催化活性最好,在360℃、3 M Pa、氫油體積比500、液時空速2 h-1的反應條件下,喹啉的脫氮率可以達到85.6%。
채용등체적침지법화H2원위환원법제비료Ni2 P/SBA‐15최화제,분별고찰료불동P/Ni비、환원온도、활성조분질량분수대가경탈담성능적영향。채용 X 사선연사(XRD )、N2흡부탈부(BET )등기술,고찰료SBA‐15분자사급기최화제형모화직구성질,병이규람위모형화합물재미형고정상반응기상고찰료불동온도대최화제가경탈담(HDN )성능적영향。결과표명,당린얼비위1,린화얼질량분수위30%,환원온도위650℃시,기최화활성최호,재360℃、3 M Pa、경유체적비500、액시공속2 h-1적반응조건하,규람적탈담솔가이체도85.6%。
The supported nickel phosphide catalysts were prepared by incipient wetness impregna‐tion and in situ H2 reduction method .The effects of the different P/Ni ratio ,reduction temperature , and active component mass fraction on the performance of hydrodenitrogenation were examined .The samples were characterized by N2 adsorption‐desorption ,X‐ray diffraction (XRD) ,and temperature‐programmed desorption of ammonia ,and the effects of different temperature on the properties of cata‐lyst hydrodenitrogenation (HDN ) w ere evaluated on a continuous‐flow fixed‐bed reactor by using quinoline as the model molecules .T he results show that w hen the nickel phosphorus ratio is 1 ,nickel phosphide mass fraction is 30% ,and the reduction temperature is 650 ℃ ,its catalytic activity is best . At a reaction temperature of 360 ℃ ,pressure of 3 MPa ,hydrogen/oil volume ratio of 500 ,and liquid hourly space velocity of 2 h-1 ,the HDN conversion of quinoline can reach 85 .6% .