从甲烷或天然气中直接生产氢和芳烃:最近美国专利的回顾

L. Petkovic, D. Ginosar
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引用次数: 4

摘要

自2000年以来,美国专利商标局(USPTO)已经授予了十几项与甲烷脱氢芳构化工艺相关的发明专利。其中一个被授予UOP LLC (Des Plaines)。本发明涉及一种催化剂组合物及其制备方法。两项专利被授予康菲石油公司(Houston, TX)。其中一项旨在确定甲烷芳构化的工艺和操作条件。另一个目标是确保一个可以与井口流体分离和从天然气中产生的芳烃与原油混合相结合的过程。9项专利被授予埃克森美孚化学专利公司(Houston, TX)。其中大多数旨在确保脱氢芳构化过程,其中含甲烷的原料目前移动到颗粒催化剂。焦化的催化剂在反应器中通过循环操作或在附属设备中加热或再生,然后返回反应器。反应器流出流可按其主要组分分离,并根据需要加以利用或再循环。本文对这些发明作一简要综述。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Direct production of hydrogen and aromatics from methane or natural gas: Review of recent U.S. patents
Since the year 2000, the United States Patent and Trademark Office (USPTO) has granted a dozen patents for inventions related to methane dehydroaromatization processes. One of them was granted to UOP LLC (Des Plaines). It relates to a catalyst composition and preparation method. Two patents were granted to Conoco Phillips Company (Houston, TX). One was aimed at securing a process and operating conditions for methane aromatization. The other was aimed at securing a process that may be integrated with separation of wellhead fluids and blending of the aromatics produced from the gas with the crude. Nine patents were granted to ExxonMobil Chemical Patents Inc. (Houston, TX). Most of these were aimed at securing a dehydroaromatization process where methane-containing feedstock moves counter currently to a particulate catalyst. The coked catalyst is heated or regenerated either in the reactor, by cyclic operation, or in annex equipment, and returned to the reactor. The reactor effluent stream may be separated in its main components and used or recycled as needed. A brief summary of those inventions is presented in this review.
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