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Catalyst Innovation Improves Commercial Application of the OATS~(TM) Process

机译:催化剂创新改善了OATS〜(TM)工艺的商业应用

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摘要

Many catalyzed reactions in the refinery are carried out in multi-phase reactors, for example in the most widely used technology for sulphur removal - the HDS (Hydrodesul-phurisaiion) process. Even if the reaction has been well known for over 40 years, the chemical process is still very complex. Temperature control as well as the scaling up of the reactor are important and problematic, e. g. leading to a complex reactor design requiring gas phase recycle with high costs for recompressing because the H2-supply needs to exceed significantly what is chemically consumed. The OATS~(TM) (= Olefin Alkylation of Thio-phenic Sulphur) process is an alternative route for sulfur removal and requires no hydrogen at all. In this non-HDS based desul-phurisation technology, organic sulphur compounds are shifted to higher boiling points and thus can be removed by distillation from the light fractions and concentrated in the heavy boiling part of the refinery streams. In 2002 the Bayernoil Refinery in Bavaria licensed OATS technical information and patents from BP Refining Technology, and built the very first two commercial OATS~(TM) plants in their Neustadt and Vohburg refineries. As with most new processes the units had some initial problems, but both units have now been successfully operated and are now producing continuously up to 200 m /h ofULSG (ultra low sulphur gasoline) with feed coming from all three of Bayernoil's FCC units. Working as a 2-phase system under mild conditions with low energy costs and without any use of metal compounds in the catalyst, ULSG with sulphur levels of < 30ppm can beproduced, allowing, the blended products to meet the most severe motor gasoline specifications (Euro 5). After the introduction of a new tailor-made catalyst provided by Axens, who are now exclusive licensors of the technology, and testing by the refinery, the process conditions, yield pattern and catalyst handling have been improved in such a way that OATS can now be considered as an excellent alternative route for the desulphurisation of mainly light fractions from FCC units without using hydrogen. In this article, the chemical fundamentals and the short history at Bayernoil are de-scribed where both the licensor and the refinery optimized the OATS~(TM)process.
机译:炼油厂中的许多催化反应都是在多相反应器中进行的,例如,最广泛使用的脱硫技术-HDS(Hydrodesul-phurisaiion)工艺。即使该反应已经众所周知了40多年,化学过程仍然非常复杂。温度控制以及反应器的按比例放大是重要且有问题的,例如。 G。导致复杂的反应器设计需要气相再循环,并且压缩成本高,因为氢气的供应量必须大大超过化学消耗量。 OATS TM(=苯硫的烯烃烷基化)方法是除硫的替代途径,根本不需要氢。在这种非基于HDS的脱硫技术中,有机硫化合物被转移到更高的沸点,因此可以通过蒸馏从轻馏分中除去,并浓缩在精炼流的重沸点部分。 2002年,巴伐利亚州的拜仁石油精炼厂从BP精炼技术获得了OATS的技术信息和专利许可,并在他们的Neustadt和Vohburg精炼厂中建立了头两个商业OATS〜(TM)工厂。与大多数新工艺一样,这些装置都存在一些最初的问题,但是两个装置现在都已经成功运行,并且连续生产高达200 m / h的ULSG(超低硫汽油),其原料来自拜仁石油公司的三个FCC装置。在温和条件下作为两相系统运行,具有较低的能源成本,并且无需在催化剂中使用任何金属化合物,可以生产硫含量<30ppm的ULSG,使混合后的产品符合最严格的汽车汽油规格(欧洲5)。引入由Axens提供的新的量身定制的催化剂(现在是该技术的独家许可人)并由炼油厂进行测试之后,工艺条件,产率模式和催化剂处理方式都得到了改进,从而可以通过OATS被认为是不使用氢气对FCC装置中的主要轻馏分进行脱硫的绝佳替代方法。在本文中,描述了许可人和精炼厂均优化OATS〜(TM)工艺的Bayernoil的化学基本原理和短暂历史。

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