无机盐工业
主管:中海油天津化工研究设计院有限公司
主办:中海油天津化工研究设计院有限公司
   中海油炼油化工科学研究院(北京)有限公司
   中国化工学会无机酸碱盐专业委员会
ISSN 1006-4990 CN 12-1069/TQ
催化材料

不同助剂对Ni/Al2O3催化顺酐液相加氢选择性的影响

  • 朱金剑 ,
  • 杨霞霞 ,
  • 穆展鹏 ,
  • 宋国良 ,
  • 李子涵 ,
  • 刘伟 ,
  • 许岩 ,
  • 张景成
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  • 1.中海油天津化工研究设计院有限公司,天津 300131
    2.中国石油大学(北京),北京 102249
朱金剑(1986— ),男,硕士,主要研究方向为炼油化工加氢技术及催化剂制备技术优化;E-mail:zhujj8@cnooc.com.cn

收稿日期: 2023-08-18

  网络出版日期: 2024-04-18

Effect of different additives on liquid phase selective hydrogenation performance of maleic anhydride over Ni/Al2O3

  • ZHU Jinjian ,
  • YANG Xiaxia ,
  • MU Zhanpeng ,
  • SONG Guoliang ,
  • LI Zihan ,
  • LIU Wei ,
  • XU Yan ,
  • ZHANG Jingcheng
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  • 1.CNOOC Tianjin Chemical Research and Design Institute Co., Ltd., Tianjin 300131, China
    2.China University of Petroleum, Beijing 102249, China

Received date: 2023-08-18

  Online published: 2024-04-18

摘要

采用超声辅助沉淀法分别使用P、Mg、Mo、Cu助剂制备了系列镍基顺酐加氢催化剂。采用N2物理吸附-脱附、X射线衍射(XRD)、氢程序升温还原(H2-TPR)、氨程序升温脱附(NH3-TPD)等方法对催化剂进行了表征分析,考察不同助剂对催化剂晶型结构、还原性能、酸强度、BET比表面积和孔结构等的影响。结果表明,助剂高度分散在催化剂体系中,同时助剂的引入使催化剂比表面积和孔容呈现不同程度的减小,此外添加助剂提高了催化剂还原温度,增强了活性金属与载体之间相互作用力,导致催化剂还原程度不同,使Ni0及具有L酸特性的Ni δ+数目不同,进而影响氢气活化及C=C/C=O键吸附能力。使用固定床顺丁烯二酸酐液相连续加氢反应对催化剂进行性能评价,结果发现,Ni-Mo/Al2O3催化剂具有最优的γ-丁内酯选择性,在反应压力为5 MPa、反应温度为150 ℃、氢酐物质的量比为5∶1、空速为1 h-1的工艺条件下,顺酐转化率为99.48%、γ-丁内酯选择性为54.34%。

本文引用格式

朱金剑 , 杨霞霞 , 穆展鹏 , 宋国良 , 李子涵 , 刘伟 , 许岩 , 张景成 . 不同助剂对Ni/Al2O3催化顺酐液相加氢选择性的影响[J]. 无机盐工业, 2024 , 56(4) : 143 -150 . DOI: 10.19964/j.issn.1006-4990.2023-0417

Abstract

A series of nickel-based maleic anhydride hydrogenation catalysts were prepared by ultrasound-assisted precipitation method using P,Mg,Mo,and Cu additives,respectively.The catalysts were characterized and analyzed by N2 physical adsorption-desorption,X-ray diffraction(XRD),programmed temperature-raising reduction(H2-TPR),and ammonia-programmed temperature-raising desorption(NH3-TPD),to investigate the effects of different additives on the crystalline structure of the catalysts,the reduction performance,acid strength,BET specific surface area and pore structure.The results showed that the additives were highly dispersed in the catalyst system,while the introduction of the additives caused the specific surface area and pore volume of the catalysts to show different degrees of reduction.In addition,the additives increased the reduction temperature of the catalysts and enhanced the interaction force between the active metals and the carriers,which led to the different degrees of reduction of the catalysts,and resulted in different numbers of Ni0 and Niδ+ with the characteristics of L-acid,which in turn affected the hydrogen activation and the adsorption capacity of the C=C/C=O bonds.The performance of the catalyst was evaluated using a fixed-bed maleic anhydride liquid-phase continuous hydrogenation reaction,and it was found that the Ni-Mo/Al2O3 catalyst had the optimal γ-butyrolactone selectivity.Under the process conditions of reaction pressure of 5 MPa,reaction temperature of 150 ℃,molar ratio of 5∶1 for hydrogen anhydride,and space velocity of 1 h-1,the conversion rate of maleic anhydride was ≥99.5%,the selectivity of γ-butyrolactone was ≥54.34%.

参考文献

1 SOLSONA V, MORALES-DE LA ROSA S, DE LUCA O, et al. Solvent additive-induced deactivation of the Cu-ZnO(Al2O3)-catalyzed γ-butyrolactone hydrogenolysis:A rare deactivation proce-ss[J]. Industrial & Engineering Chemistry Research202160(44):15999-16010.
2 ZHOU Yafen, WANG Qing, WANG Manman, et al. Promotional effect of CoO(OH) on selective hydrogenation of maleic anhydride to γ-butyrolactone over supported ruthenium catalyst[J]. China Petroleum Processing & Petrochemical Technology201517(4):96-101.
3 梁斌, 李宝岩, 金荣华, 等. γ-丁内酯的工业应用进展[J]. 上海师范大学学报(自然科学版)202150(5):629-635.
  LIANG Bin, LI Baoyan, JIN Ronghua, et al. Progress in industrial application of γ-butyrolactone[J]. Journal of Shanghai Normal University(Natural Sciences)202150(5):629-635.
4 何仕明, 王俊文, 张玮, 等. 苯氧化法制顺酐连续化生产工艺设计及评价[J]. 化学工程202250(4):73-78.
  HE Shiming, WANG Junwen, ZHANG Wei, et al. Process design and evaluation of continuous production of maleic anhydride by benzene oxidation[J]. Chemical Engineering(China)202250(4):73-78.
5 FAIZAN M, LI Yingwei, ZHANG Ruirui, et al. Progress of vanadium phosphorous oxide catalyst for n-butane selective oxidati-on[J]. Chinese Journal of Chemical Engineering202243:297- 315.
6 MüLLER M, KUTSCHERAUER M, B?CKLEIN S, et al. On the importance of by-products in the kinetics of n-butane oxidation to maleic anhydride[J]. Chemical Engineering Journal2020401:126016.
7 肖刚. 国内顺酐现状及发展趋势[J]. 聚酯工业202336(3):13-17.
  XIAO Gang. The current situation and development trend of Maleic anhydride in China[J]. Polyester Industry202336(3):13-17.
8 BAI Yang, CHERKASOV N, HUBAND S, et al. Highly selective continuous flow hydrogenation of cinnamaldehyde to cinnamyl alcohol in a Pt/SiO2 coated tube reactor[J]. Catalysts20188(2): 58.
9 WANG Jiandian, SUN Changyong, XIA Wenjun, et al. Pd/BN catalysts for highly efficient hydrogenation of maleic anhydride to succinic anhydride[J]. Applied Catalysis A:General2022630:118471.
10 LI Haoyu, WU Pengfei, LI Xianquan, et al. Catalytic hydrogenation of maleic anhydride to γ-butyrolactone over a high-performance hierarchical Ni-Zr-MFI catalyst[J]. Journal of Catalysis2022410:69-83.
11 ZHAO Lili, ZHAO Jianghong, WU Tianjie, et al. Synergistic effect of oxygen vacancies and Ni species on tuning selectivity of Ni/ZrO? catalyst for hydrogenation of maleic anhydride into succinic anhydride and γ-butyrolacetone[J]. Nanomaterials20199(3):406.
12 YU Zhiquan, WANG Anjie, LIU Shan, et al. Hydrodeoxygenation of phenolic compounds to cycloalkanes over supported nickel phosphides[J]. Catalysis Today2019319:48-56.
13 ZHOU Yafen, CHEN Qilin, WANG Qing, et al. Selective hydrogenation of maleic anhydride to succinic anhydride over nickel catalyst supported on carbon microspheres[J]. China Petroleum Processing & Petrochemical Technology202123(4):75-82.
14 REDDY KANNAPU H P, MULLEN C A, ELKASABI Y, et al. Catalytic transfer hydrogenation for stabilization of bio-oil oxygenates:Reduction of p-cresol and furfural over bimetallic Ni-Cu catalysts using isopropanol[J]. Fuel Processing Technology2015137:220-228.
15 SHEN Zhibing, KE Ming, YU Pei, et al. Catalytic activities of Mo-modified Ni/Al2O3 catalysts for thioetherification of mercaptans and di-olefins in fluid catalytic cracking naphtha[J]. Transition Metal Chemistry201237(6):587-593.
16 LI Jingfeng, CHAI Yongming, LIU Bin, et al. The catalytic performance of Ni2P/Al2O3 catalyst in comparison with Ni/Al2O3 catalyst in dehydrogenation of cyclohexane[J]. Applied Catalysis A:General2014469:434-441.
17 SHE Tiantian, CHU Xiaoning, ZHANG Huiling, et al. Ni-Mg/γ-Al2O3 catalyst for 4-methoxyphenol hydrogenation:Effect of Mg modification for improving stability[J]. Journal of Nanoparticle Research201820(9):224.
18 刘伟, 张景成, 陈永生, 等. 一种高活性镍基丙酮加氢催化剂及制备方法:中国,112337474B[P]. 2023-05-09.
19 刘伟, 陈永生, 许岩, 等. 一种羟乙基乙二胺合成哌嗪的催化剂及其制备方法、应用:中国,114247449B[P]. 2023-08-22.
20 刘伟, 许岩, 陈永生, 等. 碱土金属对铜/三氧化二铝酯加氢催化剂性能的影响[J]. 无机盐工业202355(9):140-144.
  LIU Wei, XU Yan, CHEN Yongsheng, et al. Effect of alkaline earth metals on performance of Cu/Al2O3 ester hydrogenation cat-alyst[J]. Inorganic Chemicals Industry202355(9):140-144.
21 ZHUANG Jianguo, YAN Siyan, ZHANG Peng, et al. Regulating the states of Ni species by controlling the silanols of MCM-41 support to promote the hydrogenation of maleic anhydride[J]. Fuel2023335:127030.
22 HUANG Guan, SUN Zhichao, LIU Yingya, et al. Efficient Ni2P/SiO2 catalysts with enhanced performance for the hydrogenation of 4,6-dimethyldibenzothiophene and phenanthrene[J]. Industrial & Engineering Chemistry Research202362(29):11428-11438.
23 张因, 郭健健, 王杰, 等. 以NiAl-NO3-LDH为前驱体制备Ni-Al2O3催化剂及其催化乙酰丙酸加氢性能[J]. 高等学校化学学报201940(8):1686-1696.
  ZHANG Yin, GUO Jianjian, WANG Jie, et al. Preparation of Ni-Al2O3 catalysts derived from hydrotalcite and its catalytic performance for hydrogenation of levulinic acid[J]. Chemical Journal of Chinese Universities201940(8):1686-1696.
24 TIAN Weiping, GUO Shaofei, SHI Li. Ni-loaded catalyst containing activated clay for maleic anhydride hydrogenation to succinic anhydride[J]. China Petroleum Processing & Petrochemical Technology201113(4):35-40.
25 CHU Shuang, LI Xiang, ZHOU Xuerong, et al. Preparation of Ni2P supported on Al2O3 and B2O3 mixed oxides by temperature-programmed reduction of phosphate precursors with low P/Ni ratios[J]. Topics in Catalysis202063(15):1379-1387.
26 LI Xiang, FENG Jianpeng, GUO Jingyu, et al. Preparation of Ni2P/Al2O3 by temperature-programmed reduction of a phosphate precursor with a low P/Ni ratio[J]. Journal of Catalysis2016334:116-119.
27 ZHANG Zhena, TANG Mingxiao, CHEN Jixiang. Effects of P/Ni ratio and Ni content on performance of γ-Al2O3-supported nickel phosphides for deoxygenation of methyl laurate to hydrocarbo-ns[J]. Applied Surface Science2016360:353-364.
28 LI Kelun, WANG Rijie, CHEN Jixiang. Hydrodeoxygenation of anisole over silica-supported Ni2P,MoP,and NiMoP catalys- ts[J]. Energy & Fuels201125(3):854-863.
29 CECILIA J A, JIMéNEZ-MORALES I, INFANTES-MOLINA A, et al. Influence of the silica support on the activity of Ni and Ni2P based catalysts in the hydrodechlorination of chlorobenzene.Study of factors governing catalyst deactivation[J]. Journal of Molecular Catalysis A:Chemical2013368-369:78-87.
30 LEE Y K, OYAMA S T. Bifunctional nature of a SiO2-supported Ni2P catalyst for hydrotreating:EXAFS and FTIR studies[J]. Journal of Catalysis2006239(2):376-389.
31 LONG Huali, XU Yan, ZHANG Xiaoqing, et al. Ni-Co/Mg-Al catalyst derived from hydrotalcite-like compound prepared by plasma for dry reforming of methane[J]. Journal of Energy Chemistry201322(5):733-739.
32 SAWHILL S J, LAYMAN K A, VAN WYK D R, et al. Thiophene hydrodesulfurization over nickel phosphide catalysts:Effect of the precursor composition and support[J]. Journal of Catalysis2005231(2):300-313.
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