...
首页> 外文期刊>Fuel >Bio-oil hydrotreating over conventional CoMo & NiMo catalysts: The role of reaction conditions and additives
【24h】

Bio-oil hydrotreating over conventional CoMo & NiMo catalysts: The role of reaction conditions and additives

机译:常规CoMo和NiMo催化剂上的生物油加氢处理:反应条件和添加剂的作用

获取原文
获取原文并翻译 | 示例
           

摘要

Wood-derived bio-oil was investigated as a feedstock for the production of renewable hydrocarbons over commercial hydrotreating CoMoS and NiMoS catalysts. Alumina-supported CoMoS active phase showed better selectivity to diesel-like products than NiMoS phase and higher activity in removal of gaseous intermediates (COx) by hydrogenation. This reaction can play an important role in the reduction of corrosivity at the reactor outlet and determine the process economy. The disadvantage of alumina as a support material was its low stability at high temperatures in presence of water. NiMoS catalyst was found to be more active in decarboxylation and it was possible to reach a steady state production of hydrocarbons having a comparable boiling point distribution with crude oil middle distillates. A test performed with a combination of NiMoS (at the top of the catalyst bed) and CoMoS (at the bottom of the reactor) revealed the key role of the catalyst type and reaction conditions in the first zone of the reactor. The experiments with elevated feeding rates showed the undesirable presence of the not-stabilized reactants behind the first reactor zone. Reaction conditions, catalyst selection and presence of additives (methanol to modify viscosity, DMDS/H2S to stabilize active centers) were combined and optimized to tune the product composition and properties. The catalyst low-temperature activity in the first reactor zone was the limiting factor for the maximum feed rate and reactor capacity. The reaction temperature in this zone strongly affects the boiling point distribution of the product. In case of NiMo catalyst, the reaction temperature above 360 C-omicron in the 3rd zone can reduce molecular weight of the product due to mild cracking. In contrast, temperatures above 400 C-omicron result in fast deactivation preventing thus the establishment of the steady state operating regime. (C) 2016 Elsevier Ltd. All rights reserved.
机译:木材衍生的生物油已被用作在商业加氢处理CoMoS和NiMoS催化剂上生产可再生碳氢化合物的原料。氧化铝负载的CoMoS活性相显示出比NiMoS相更好的对柴油样产物的选择性,并具有通过氢化去除气态中间体(COx)的更高活性。该反应可以在降低反应器出口的腐蚀性和确定工艺经济性方面发挥重要作用。氧化铝作为载体材料的缺点是在高温下有水存在时稳定性低。发现NiMoS催化剂在脱羧中更具活性,并且有可能达到稳态生产的烃,其沸点分布与原油中间馏分相当。用NiMoS(在催化剂床的顶部)和CoMoS(在反应器的底部)的组合进行的测试揭示了催化剂类型和反应条件在反应器第一个区域中的关键作用。进料速率提高的实验表明,在第一反应器区域后不希望有的不稳定反应物的存在。将反应条件,催化剂选择和添加剂(甲醇以改变粘度,DMDS / H2S以稳定活性中心)的存在相结合并进行优化以调整产品组成和性能。在第一反应器区域中的催化剂低温活性是最大进料速率和反应器容量的限制因素。在该区域中的反应温度强烈影响产物的沸点分布。在使用NiMo催化剂的情况下,第三区的反应温度高于360 C微米会由于温和裂解而降低产物的分子量。相反,高于400℃-微米的温度导致快速失活,从而阻止建立稳态工作状态。 (C)2016 Elsevier Ltd.保留所有权利。

著录项

  • 来源
    《Fuel》 |2017年第15期|49-57|共9页
  • 作者

    Horacek Jan; Kubicka David;

  • 作者单位

    Unipetrol Ctr Res & Educ, Block 2838, Litvinov Zaluzi 43670 1, Czech Republic;

    Univ Chem & Technol Prague, Technopk Kralupy VSCHT Praha, Zizkova 7, Kralupy Nad Vltavou 27801, Czech Republic;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Bio-oil; Deoxygenation; Hydrotreating;

    机译:生物油;脱氧;加氢处理;

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号