[1]樊宏飞,孙晓艳,于政敏,等.加氢裂化催化剂FC-38的性能及应用[J].石化技术与应用,2022,2:73-77.
FAN Hong-fei,SUN Xiao-yan,YU Zheng-min,et al.Performance and application of hydrocracking catalyst FC-38[J].Petrochemical technology & application,2022,2:73-77.
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《石化技术与应用》[ISSN:1009-0046/CN:62-1138/TQ]
- 期数:
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2022年2期
- 页码:
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73-77
- 栏目:
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- 出版日期:
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2022-03-10
文章信息/Info
- Title:
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Performance and application of hydrocracking catalyst FC-38
- 作者:
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樊宏飞; 孙晓艳; 于政敏; 陈玉晶*
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中国石化大连石油化工研究院,辽宁 大连 116045
- Author(s):
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FAN Hong-fei; SUN Xiao-yan; YU Zheng-min; CHEN Yu-jing
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Dalian Research Institute of Petroleum and Petrochemical, SINOPEC, Dalian 116045,China
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- 关键词:
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Al-SBA-15; Y型分子筛; 加氢裂化; 催化剂; 中间馏分油; 航空煤油
- Keywords:
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Al-SBA-15; Y zeolite; hydrocracking; catalyst; middle-distillate; aviation kerosene
- 分类号:
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TE 624.9
- DOI:
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DOI:10.19909/j.cnki.ISSN1009-0045.2022.02.0073
- 文献标识码:
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B
- 摘要:
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以新型介孔材料Al-SBA-15与深度改性Y型分子筛复合后得到的微介孔复合分子筛作为主要酸性组分,钨镍为加氢组分,开发了单段高中油型加氢裂化催化剂FC-38,考察了其物化性质、反应性能与工业应用效果,并与FC-34的性能进行了对比。结果表明:壳层Al的引入在不影响分子筛水热稳定性的同时提供了弱酸性位;与单一Y型分子筛相比,Al-SBA-15/Y试样的比表面积和孔体积显著增加,B酸量和L酸量均减少;在相同转化率条件下,与FC-34相比,FC-38的反应温度降低2 ℃以上,中间馏分油选择性提高2.1个百分点,柴油十六烷值增加,尾油芳烃指数降低;在工业装置生产中,催化剂FC-38的活性稳定,加氢裂化产品质量均达到或超过技术协议的指标要求。其中:航空煤油馏分烟点均超过26 mm,可直接作为优质3#航空煤油;加氢裂化尾油可作为优质的润滑油基础油原料或催化裂化原料。
- Abstract:
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A single-stage high and middle-distillate hydrocracking catalyst FC-38 was developed with micro and mesopore composite zeolite which contained the new mesopore material Al-SBA-15 and deep modified Y zeolite as main acidity component and tungsten and nickel as hydrogenation component. The catalyst′s properties, catalytic performance and industrial application were investigated and were compared with those of FC-34. The result showed that the introduction of shell Al had provided weak acidity without affecting the hydrothermal stability of zeolite. Compared with adopting Y zeolite solely, the Al-SBA-15/Y composite zeolite possessed larger specific surface area and pore volume while containing less B and L acidic sites. Under the same conversion, the reaction temperature of FC-38 catalyst was 2 ℃ lower than that of FC-34 catalyst. The selectivity of middle-distillate of FC-38 catalyst had increased by 2.1 percentage points, the cetane value of diesel oil was higher and the BMCI of tail oil was lower when compared with that of FC-34 catalyst. In industrial units, the activity of catalyst FC-38 was stable and the quality of all hydrocracking products had met/exceeded the requirements of technical agreement. The smoke point of aviation kerosene fraction was more than 26 mm, which could be directly used as high quality 3# aviation kerosene. The hydrocracking tail oil could be used as high quality lubricating base oil raw material or catalytic cracking raw material.
参考文献/References
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[3] 倪术荣, 赵檀, 王燕,等. 国外馏分油加氢裂化催化剂研究进展[C]. 第十二届全国工业催化技术及应用年会, 2015.
[4] 武宝萍, 沈健, 张秋荣. 微孔-介孔复合分子筛HY-SBA-15的表征及应用[J]. 燃料化学学报, 2012, 40 (6):732-736.
[5] 樊宏飞, 孙晓艳, 徐学军,等. 单段加氢裂化催化剂的开发及应用[J]. 炼油技术与工程, 2005,35 (7):36-40.
[6] 樊宏飞, 孙晓艳, 关明华,等. FC-26中间馏分油型选择性加氢裂化催化剂的研究[J]. 石油炼制与化工, 2005, 36 (2):9-11.
[7] 田洪良, 潘德满. FC-40高中油型加氢裂化催化剂的反应性能研究[J]. 当代化工, 2008, 37 (1):54-56.
更新日期/Last Update:
2022-03-10