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Catalytic syntheses with high yields - suitable for mfg. ammonia, methane, methanol, or the conversion of carbon monoxide

机译:高产率的催化合成-适用于制造。氨,甲烷,甲醇或一氧化碳的转化

摘要

A reversible, exothermic, gas-phase reaction is undertaken where a gas stream contg. one or more reactants is fed through =1 catalyst zones to obtain =1 prods. The gas stream is fed at temp. (T1) into a first reaction zone (R1) using adiabatic conditions so as higher temp. (T2) is attained; T2 is lower than the inactivation temp. of the catalyst. The gas at T2 then flows into a second zone (R2) provided with continuous external cooling to obtain a prod. mixt. leaving zone (R2) at temp. (T3) which is lower than T2. The gas may be recycled through the process and T3 is pref. max. T1. The initial gas is pref. a mixt. of (a) N2 and H2 for mfg. NH3; or (b) H2 and CO for mfg. methanol; or (c) COx and H2 for mfg. methane; or (d) H2 and CO, and using a CO conversion catalyst. Improved yields in the synthesis of cpds. such as CH3 OH or NH3 are obtd. For example, the % of NH3 in the outlet gas can be raised to 20% c.f. 16.5-17.5% obtd. in conventional processes.
机译:在气流连续的情况下进行可逆的放热气相反应。将一种或多种反应物送入> = 1个催化剂区域,以获得> = 1个产品。气流在温度下进料。 (T1)使用绝热条件进入较高温度的第一反应区(R1)。 (T2)已达到; T2低于失活温度。催化剂。然后,在T2处的气体流入第二个区域(R2),该区域设有连续的外部冷却以获得产品。混音在温度下离开区域(R2)。 (T3)低于T2。可以通过该过程将气体再循环,并且T 3是优选的。最高T1。初始气体为优选。混音。 (a)N2和H2的mfg。 NH3;或(b)氢气和一氧化碳制造。甲醇或(c)mfg的COx和H2。甲烷(d)H 2和CO,并使用CO转化催化剂。 cpds合成中产率提高。如CH3 OH或NH3。例如,出口气体中NH3的百分比可以提高到20%c.f.。增长16.5-17.5%在常规过程中。

著录项

  • 公开/公告号DE2705673A1

    专利类型

  • 公开/公告日1977-08-18

    原文格式PDF

  • 申请/专利权人 DAVY POWERGAS LTD.;

    申请/专利号DE19772705673

  • 发明设计人 ESWARD HARDWICKWILLIAM;

    申请日1977-02-11

  • 分类号B01J1/14;C01C1/04;C01B2/06;C07C31/06;C07C9/04;C07C1/16;

  • 国家 DE

  • 入库时间 2022-08-22 23:57:46

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