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Methanol prepd. with lower energy requirements - by catalytic cleavage of hydrocarbons, followed by synthesis of methanol from hydrogen and carbon oxides obtd.

机译:甲醇制备。具有较低的能源需求-通过碳氢化合物的催化裂解,然后由氢和碳氧化物合成甲醇。

摘要

The prepn. of methanol from gaseous and liq. hydrocarbons (I) with a C/H ratio higher than that stoichiometrically reqd. for methanol prodn. by (i) catalytic cleavage of (I) in one- or 2-step process by the addn. of steam at 350-900 degrees C and 5-30 bar to give a gas consisting essentially of H2 and oxides of carbon and (ii) catalytic synthesis of methanol from H2 and oxides of carbon at 230-280 degrees C and 30-150 bar, is improved by removing carbon-contg. gaseous components (II) from the waste-gas from step (ii) and mixing the remaining H2-rich gaseous components (III) with (I) provided that the resulting mixt. has C/H ratio is not 5.7. Pref. (II) are removed without expenditure of energy esp. by using a mol. sieve. The heat/energy requirements (based on MeOH prodn.) are lowered. The deleterious effects of by-products (esp. high-boiling aromatics) is reduced, the catalysts have a longer life. It is also possible to use S-contg. starting materials; as part or all of (III) can be used to remove sulphur from (I) by hydrogenation. (II) consists primarily of CO2,CO and CH4 and can be used to heat (I) before the second catalytic cleavage step.
机译:的准备。来自气态和液态的甲醇C / H比高于化学计量要求的碳氢化合物(I)。用于甲醇产品通过(i)通过加成反应以一步或两步方法催化裂解(I)。在350-900摄氏度和5-30巴的压力下产生蒸汽,从而产生一种基本由H2和碳氧化物组成的气体;(ii)在230-280摄氏度和30-150巴的条件下由H2和碳的氧化物催化合成甲醇通过去除积碳可改善。来自步骤(ii)的废气中的气态组分(II),并将剩余的富H2气态组分(III)与(I)混合,以确保得到最终混合物。 C / H比不大于5.7。首选(II)无需花费能量特别是被去除。通过使用摩尔。筛。降低了热/能量要求(基于MeOH产品)。副产物(尤其是高沸点芳烃)的有害作用降低,催化剂寿命更长。也可以使用S-contg。起始原料; (III)的一部分或全部可用于通过氢化从(I)中除去硫。 (II)主要由CO2,CO和CH4组成,可在第二个催化裂解步骤之前用于加热(I)。

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