Industrial Techniques

Industrial application of THFS-2 sulfurized reforming prehydrogenation catalysts

  • WANG Chao ,
  • SONG Guoliang ,
  • XIAO Han
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  • 1.CNOOC Huizhou Petrochemical Company Limited, Huizhou 516086, China
    2.CenterTech Tianjin Chemical Research and Design Institute Co. Ltd. , Tianjin 300131

Received date: 2023-12-08

  Online published: 2024-05-15

Abstract

According to the demand on hydrogenation of the high nitrogen and naphthenic base of traight naphtha for reforming raw materials,THFS-2 sulfurized reforming pre-hydrogenation catalyst was developed through the independently developed in-situ activation technique.The catalysts were characterized by BET,H2-TPR,XRD,NH3-TPD,Py-FTIR and TEM techniques.The results showed that compared to the THFS-1 hydrogenation catalyst,the addition of organic phosphorus assistant optimized the pore structure of the catalyst,increased the distributions of medium strong acid and B acid,improved the metal sulfide and atomic utilization rate,and formd more active “NiMoS-Ⅱ” phases.THFS-2 catalyst achieved industrial application on 800 000 t/a reforming pre-hydrogenation unit of CNOOC Huizhou Petrochemical Co.,Ltd.The activation process was more efficient and environmentally friendly,the activation time was reduced to 18 h,and the highest hydrogen sulfide content in recycle hydrogen was less than 2 000 μg/g.Under the full load conditions of reaction inlet temperature of 289 ℃,hydrogen partial pressure of 2.4 MPa,the GHSV of 5.0 h-1,and hydrogen-oil ratio of 130 Nm3/m3,the sulfur and nitrogen contents in hydrogenated naphtha were less than 0.5 μg/g,the bromine index was less than 100 mg/100 g,the arsenic content was less than 1.0 µg/kg,and the chlorine content was less than 0.5 µg/g.The result of industrial operation showed that THFS-2 sulfurized reforming prehydrogenation catalyst had excellent performance.It could meet the hydrogenation activity of the high nitrogen straight-run naphtha under the condition of high GHSV,and provided qualified raw materials for reforming plant.

Cite this article

WANG Chao , SONG Guoliang , XIAO Han . Industrial application of THFS-2 sulfurized reforming prehydrogenation catalysts[J]. Inorganic Chemicals Industry, 2024 , 56(5) : 94 -100 . DOI: 10.19964/j.issn.1006-4990.2023-0593

References

1 慕彦君,宋倩倩,付凯妹,等.芳烃生产技术进展及产业发展建议[J].石化技术与应用202139(5):371-377.
  MU Yanjun, SONG Qianqian, FU Kaimei,et al.Progress and industrial development suggestion of aromatics production technology[J].Petrochemical Technology & Application202139(5):371-377.
2 辛靖,高杨,侯章贵,等.以生产轻芳烃为目的的催化重整装置原料拓展研究进展[J].无机盐工业201951(7):1-7.
  XIN Jing, GAO Yang, HOU Zhanggui,et al.Research progress on expanding feedstocks for catalytic reforming units for the production of light aromatics[J].Inorganic Chemicals Industry201951(7):1-7.
3 ANCHEYTA-JUáREZ J, VILLAFUERTE-MACíAS E.Kinetic modeling of naphtha catalytic reforming reactions[J].Energy & Fuels200014(5):1032-1037.
4 李洪亮,冯连坤,陈晓华.催化重整联合装置减油增化措施[J].石化技术与应用202341(4):315-319.
  LI Hongliang, FENG Liankun, CHEN Xiaohua.Measures of reducing oil and increasing chemicals in catalytic reforming complex unit[J].Petrochemical Technology & Application202341(4):315-319.
5 马致远,王辉,王文辰,等.催化裂化汽油馏分切割作连续重整原料生产芳烃[J].石化技术与应用202341(6):456-460.
  MA Zhiyuan, WANG Hui, WANG Wenchen,et al.Catalytic cracking gasoline fraction cutting as continuous reforming feedstock for producing aromatics[J].Petrochemical Technology & Application202341(6):456-460.
6 ZHANG Tiezhen, JIA Yungang, SUN Famin,et al.Preparation and performance evaluation of reforming prehydrogenation catalyst used for blending inferior coking gasoline[J].International Journal of Power and Energy Research20204(3):27-33.
7 王健,朱俊华,叶迎春,等.载体预处理对Mo/Al2O3催化剂催化裂解汽油加氢脱氮性能的影响[J].化学反应工程与工艺202339(4):306-312.
  WANG Jian, ZHU Junhua, YE Yingchun,et al.Effect of support treatment on hydrodenitrogenation performance for pyrolysis gasoline over Mo/Al2O3 catalysts[J].Chemical Reaction Engineering and Technology202339(4):306-312.
8 刘帅,白鸿博.柴油加氢工艺及催化剂研究进展[J].当代化工202352(9):2237-2242.
  LIU Shuai, BAI Hongbo.Research progress of diesel hydrogenation reaction process and hydrogenation catalysts[J].Contemporary Chemical Industry202352(9):2237-2242.
9 RAHIMPOUR M R, JAFARI M, IRANSHAHI D.Progress in catalytic naphtha reforming process:A review[J].Applied Energy2013109:79-93.
10 胡明涛,王德胜.浅谈芳烃联合装置原料变化对芳烃产品产率的影响[J].化工管理2020(9):182-183.
  HU Mingtao, WANG Desheng.Discussion on the influence of raw material change on aromatic hydrocarbon product yield in aromatic hydrocarbon combined plant[J].Chemical Enterprise Management2020(9):182-183.
11 张春生.连续重整装置掺炼焦化石脑油可行性研究[J].炼油技术与工程202353(4):5-8.
  ZHANG Chunsheng.Feasibility study on blending coking naphtha in continuous catalytic reforming unit[J].Petroleum Refinery Engineering202353(4):5-8.
12 王仲义,闫作杰,单敏,等.器外预硫化加氢裂化催化剂开工技术应用总结[J].炼油技术与工程202151(1):10-12,32.
  WANG Zhongyi, YAN Zuojie, SHAN Min,et al.Application summary of start-up technology of ex-situ presulfiding hydrocracking catalyst[J].Petroleum Refinery Engineering202151(1):10-12,32.
13 MANSUR D,AMINUDDIN.Chemical conversion of calophyllum inophyllum oil into bio-hydrocarbons fuel over presulfided NiMo/Al2O3 catalyst[J].International Journal of Energy Research202044(9):7746-7760.
14 ZHOU Lin, LAWAL A.Evaluation of presulfided NiMo/γ-Al2O3 for hydrodeoxygenation of microalgae oil to produce green diesel[J].Energy & Fuels201529(1):262-272.
15 彭雪峰,于海斌,宋国良,等.器外预硫化型加氢催化剂的制备与性能研究[J].无机盐工业201951(11):78-81.
  PENG Xuefeng, YU Haibin, SONG Guoliang,et al.Preparation and properties of ex-situ presulfurization hydrogenation catalyst[J].Inorganic Chemicals Industry201951(11):78-81.
16 李洪标,梁宇,吴显军,等.预硫化型石蜡加氢精制催化剂加氢技术研究[J].炼油与化工202233(6):21-24.
  LI Hongbiao, LIANG Yu, WU Xianjun,et al.Study on hydrogenation technology of prevulcanized paraffin hydrofining catalyst[J].Refining and Chemical Industry202233(6):21-24.
17 罗树权,孙征,高雪.加氢催化剂器外预硫化技术现状[J].化工技术与开发201443(8):34-37.
  LUO Shuquan, SUN Zheng, GAO Xue.Current situation of ex-situ pre-sulfiding hydrotreatment catalyst[J].Technology & Development of Chemical Industry201443(8):34-37.
18 彭雪峰,于海斌,张景成,等.THFS-I硫化型重整预加氢催化剂的首次工业应用[J].石油炼制与化工201748(2):68- 71.
  PENG Xuefeng, YU Haibin, ZHANG Jingcheng,et al.Industrial application of sulfide-type pre-hydrogenation catalyst THFS-I for reforming unit[J].Petroleum Processing and Petrochemicals201748(2):68-71.
19 彭雪峰,于海斌,张景成,等.THFS-Ⅰ硫化型重整预加氢催化剂的开发与性能研究[J].无机盐工业201749(2):82-86.
  PENG Xuefeng, YU Haibin, ZHANG Jingcheng,et al.Preparation and properties of THFS-Ⅰ sulfide-type reforming pre-hydrogenation catalyst[J].Inorganic Chemicals Industry201749(2):82-86.
20 彭雪峰,于海斌,孙彦民,等.THFS-I硫化型加氢催化剂在80万t·a-1重整预加氢装置上的工业运行情况[J].当代化工202251(4):989-992.
  PENG Xuefeng, YU Haibin, SUN Yanmin,et al.Industrial application of THFS-I sulfide-type hydrogenation catalyst in the 0.8 Mt·a-1 reforming pre-hydrogenation unit[J].Contemporary Chemical Industry202251(4):989-992.
21 彭雪峰,于海斌,孙彦民,等.THFS-2硫化型加氢催化剂的工业应用[J].化学工程师202236(5):75-78.
  PENG Xuefeng, YU Haibin, SUN Yanmin,et al.Industrial application of THFS-2 sulfide-type hydrogenation catalyst[J].Chemical Engineer202236(5):75-78.
22 王甫村,朱金玲,田然,等.用于FCC柴油加氢改质的选择性开环催化剂研究进展[J].化工进展201130(9):1951-1955.
  WANG Fucun, ZHU Jinling, TIAN Ran,et al.Advances in selective ring opening catalysts for FCC diesel hydro-upgrading[J].Chemical Industry and Engineering Progress201130(9):1951-1955.
23 郭振雪,于海斌,张国辉,等.Si改性对NiMo/Al2O3催化剂加氢脱硫性能的影响[J].化工进展202241(S1):210-220.
  GUO Zhenxue, YU Haibin, ZHANG Guohui,et al.Effect of Si modification on hydrodesulfurization performance of NiMo/Al2O3 catalyst[J].Chemical Industry and Engineering Progress202241(S1):210-220.
24 汪佩华,秦志峰,吴琼笑,等.磷添加方式对NiMo/Al2O3催化剂加氢脱硫性能的影响[J].化工进展202140(2):890-900.
  WANG Peihua, QIN Zhifeng, WU Qiongxiao,et al.Effect of phosphorus adding manners on the performance of NiMo/Al2O3 catalyst in hydrodesulfurization[J].Chemical Industry and Engineering Progress202140(2):890-900.
25 LIU Bin, LIU Lei, WANG Zhong,et al.Effect of hydrogen spillover in selective hydrodesulfurization of FCC gasoline over the CoMo catalyst[J].Catalysis Today2017282:214-221.
26 GUTIéRREZ O Y, KLIMOVA T.Effect of the support on the high activity of the(Ni)Mo/ZrO2-SBA-15 catalyst in the simultaneous hydrodesulfurization of DBT and 4,6-DMDBT[J].Journal of Catalysis2011281(1):50-62.
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