首页> 外国专利> Process for the reduction of NH.sub.3 in regeneration zone off gas by select recycle of certain-sized NH.sub.3 decomposition catalysts

Process for the reduction of NH.sub.3 in regeneration zone off gas by select recycle of certain-sized NH.sub.3 decomposition catalysts

机译:通过选择再循环一定尺寸的NH 3分解催化剂来减少再生区废气中NH 3的方法

摘要

This process discloses a reduction in the content of ammonia in a regeneration zone off gas of a fluid catalytic cracking unit by the select recycle of certain sized ammonia decomposition catalyst particles. The ammonia decomposition may be aided by injection of NO.sub.x into the off gas. The particles are acquired from a separation means through which is passed the regeneration zone off gas. A solid-free regeneration zone off gas and a stream of solid particles, including a noble metal dispersed on an inorganic support, having a size of from 10 to 40 microns, are acquired. The latter segregated particles are then injected into the regeneration zone at a predetermined make-up rate to insure a very short residence time in the dense phase of the regeneration zone and to provide a relatively constant concentration of the NH.sub.3 decomposition catalyst in the dilute phase of the regeneration zone to convert NH.sub.3 to N.sub.2 and water vapor. The regeneration zone is operated in a partial combustion mode defined by a CO content of from 1 to 6 percent by volume.
机译:该方法公开了通过选择再循环某些尺寸的氨分解催化剂颗粒来减少流体催化裂化单元的再生区废气中的氨含量。氨分解可以通过将NO x注入废气中来辅助。颗粒从分离装置中获取,再生区废气通过分离装置。获得了无固体的再生区废气和固体颗粒流,包括分散在无机载体上的贵金属,该固体颗粒流的尺寸为10至40微米。然后将后分离的颗粒以预定的补充速率注入再生区中,以确保在再生区的密相中的停留时间非常短,并在其中提供相对恒定浓度的NH.3分解催化剂。再生区的稀相将NH3转化为N2和水蒸气。再生区以部分燃烧模式运行,该部分燃烧模式的CO含量为1-6%(体积)。

著录项

  • 公开/公告号US4755282A

    专利类型

  • 公开/公告日1988-07-05

    原文格式PDF

  • 申请/专利权人 SHELL OIL COMPANY;

    申请/专利号US19870076470

  • 发明设计人 JOHN E. GWYN;NORMAN C. SAMISH;

    申请日1987-07-22

  • 分类号C06;B01J8/02;

  • 国家 US

  • 入库时间 2022-08-22 06:48:55

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