石油炼制与化工
石油煉製與化工
석유련제여화공
PETROLEUM PROCESSING AND PETROCHEMICALS
2015年
6期
57-62
,共6页
肖寒%于海斌%张玉婷%臧甲忠
肖寒%于海斌%張玉婷%臧甲忠
초한%우해빈%장옥정%장갑충
乙二醇%Ni-W/Al2 O3%加氢脱氮%焦化轻蜡油%催化剂
乙二醇%Ni-W/Al2 O3%加氫脫氮%焦化輕蠟油%催化劑
을이순%Ni-W/Al2 O3%가경탈담%초화경사유%최화제
ethylene glycol%Ni-W/Al2 O3%hydrodenitrogenation%light coking VGO%catalyst
以 Ni、W 为活性组分,Al2 O3为载体,制备催化剂 Ni-W/Al2 O3,并采用乙二醇后处理未焙烧的催化剂 Ni-W/Al2 O3,得到催化剂 Ni-W/Al2 O3-AT 。通过 X 射线衍射(XRD)、氢气程序升温还原(H2-TPR)、紫外拉曼光谱(LRS)、透射扫描电子显微镜(TEM)、XPS 等表征方法研究催化剂的物化性质。结果表明:催化剂 Ni-W/Al2 O3经乙二醇后处理后,改善了载体氧化铝表面的羟基基团的分布,促使 W 物种以八面体配位多核聚钨酸的形态存在;并有效削弱了载体与活性金属之间的强相互作用,提高了 W 物种的分散度与硫化度,最终使得催化剂形成更多“Ni-W-S”加氢活性相,提高了催化剂 Ni-W/Al2 O3-AT 的加氢活性。与催化剂 Ni-W/Al2 O3相比,催化剂Ni-W/Al2 O3-AT 对焦化轻蜡油具有更高的加氢脱硫、脱氮与芳烃饱和性能,硫质量分数可从6850μg/g 降至10μg/g,氮质量分数由3720μg/g 降至12μg/g,双环以上芳烃质量分数可从25.8%降至3.2%。
以 Ni、W 為活性組分,Al2 O3為載體,製備催化劑 Ni-W/Al2 O3,併採用乙二醇後處理未焙燒的催化劑 Ni-W/Al2 O3,得到催化劑 Ni-W/Al2 O3-AT 。通過 X 射線衍射(XRD)、氫氣程序升溫還原(H2-TPR)、紫外拉曼光譜(LRS)、透射掃描電子顯微鏡(TEM)、XPS 等錶徵方法研究催化劑的物化性質。結果錶明:催化劑 Ni-W/Al2 O3經乙二醇後處理後,改善瞭載體氧化鋁錶麵的羥基基糰的分佈,促使 W 物種以八麵體配位多覈聚鎢痠的形態存在;併有效削弱瞭載體與活性金屬之間的彊相互作用,提高瞭 W 物種的分散度與硫化度,最終使得催化劑形成更多“Ni-W-S”加氫活性相,提高瞭催化劑 Ni-W/Al2 O3-AT 的加氫活性。與催化劑 Ni-W/Al2 O3相比,催化劑Ni-W/Al2 O3-AT 對焦化輕蠟油具有更高的加氫脫硫、脫氮與芳烴飽和性能,硫質量分數可從6850μg/g 降至10μg/g,氮質量分數由3720μg/g 降至12μg/g,雙環以上芳烴質量分數可從25.8%降至3.2%。
이 Ni、W 위활성조분,Al2 O3위재체,제비최화제 Ni-W/Al2 O3,병채용을이순후처리미배소적최화제 Ni-W/Al2 O3,득도최화제 Ni-W/Al2 O3-AT 。통과 X 사선연사(XRD)、경기정서승온환원(H2-TPR)、자외랍만광보(LRS)、투사소묘전자현미경(TEM)、XPS 등표정방법연구최화제적물화성질。결과표명:최화제 Ni-W/Al2 O3경을이순후처리후,개선료재체양화려표면적간기기단적분포,촉사 W 물충이팔면체배위다핵취오산적형태존재;병유효삭약료재체여활성금속지간적강상호작용,제고료 W 물충적분산도여류화도,최종사득최화제형성경다“Ni-W-S”가경활성상,제고료최화제 Ni-W/Al2 O3-AT 적가경활성。여최화제 Ni-W/Al2 O3상비,최화제Ni-W/Al2 O3-AT 대초화경사유구유경고적가경탈류、탈담여방경포화성능,류질량분수가종6850μg/g 강지10μg/g,담질량분수유3720μg/g 강지12μg/g,쌍배이상방경질량분수가종25.8%강지3.2%。
Ni-W/Al2 O3 catalyst was prepared by loading Ni-W metals on Al2 O3 support,and Ni-W/Al2 O3-AT catalyst was prepared by post-treating the uncalcinated Ni-W/Al2 O3 catalyst with glycol solu-tion.The physicochemical properties of the post-treated catalysts were characterized by XRD,H2-TPR, TEM,XPS and UV Raman spectroscopy (LRS).The results show that ethylene glycol not only pro-motes W species to form octahedral coordinated multi-core polytungstic acid by improving the distribu-tion of hydroxyl on the Al2 O3 support surface,but also increases the dispersion and sulfidation degree of W species on the Ni-W/Al2 O3-AT catalyst by weakening the interaction between Al2 O3 support and active metals,resulting in more “Ni-W-S”active phase and higher hydrogenation performance of post-treated catalyst.The Ni-W/Al2 O3-AT catalyst shows higher HDS,HDN and aromatics saturation per-formance than that of Ni-W/Al2 O3 catalyst for the light coking VGO.The sulfur and nitrogen contents can be reduced from 6 850 μg/g and 3 720 μg/g in feed to 10 μg/g and 12 μg/g in product,respectively, the aromatics with ≥2 rings are reduced from 25.8% to 3.2%.