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    • 144. 发明授权
    • Production of cleaned and purified synthesis gas and carbon monoxide
    • 净化和纯化的合成气和一氧化碳的生产
    • US4110359A
    • 1978-08-29
    • US749657
    • 1976-12-10
    • Charles P. Marion
    • Charles P. Marion
    • C07C29/15B01J23/00B01J23/80B01J23/86B01J23/882B01J27/00B01J31/00C01B3/36C07B61/00C07C27/00C07C29/151C07C29/153C07C29/154C07C31/04C07C51/00C07C51/12C07C53/08C07C67/00C10G9/00C10J3/00C10J3/48C07C27/06C01B2/16C07C29/16C07C51/10
    • C10J3/485B01J23/80B01J23/862B01J23/882C07C29/1512C07C29/1518C07C29/154C07C51/12C10J3/84C10K1/004C10K1/005C10K1/101C10K3/04C10J2300/16C10J2300/1665Y02P20/52Y02P30/44
    • A continuous process for simultaneously producing a stream of cleaned purified synthesis gas having a mole ratio H.sub.2 /CO in the range of about 2 to 12, and a separate stream of CO-rich gas. In one embodiment of the process, cleaned and purified methanol synthesis gas and substantially pur carbon monoxide are produced. Methanol may be synthesized and optionally catalytically reacted with the substantially pure carbon monoxide to produce acetic acid. In the subject process, the effluent gas stream directly from a free-flow unpacked noncatalytic partial-oxidation synthesis gas generator is split into two streams which are simultaneously processed in two separate trains. In the first train, one of the split streams is cooled by indirect heat exchange in a gas cooler and then further processed to produce a stream of cleaned and purified synthesis gas, a H.sub.2 -rich gas stream, and the product stream of CO-rich gas and preferably substantially pure CO. Simultaneously, the second split stream in the second train is cooled by direct quenching in water in a quench drum, cleaned, subjected to catalytic water-gas-shift reaction, and purified to produce a second H.sub.2 -rich gas stream. The product stream of cleaned and purified synthesis gas having a mole ratio H.sub.2 /CO in the range of about 2 to 12 is then produced by mixing together at least a portion of the cleaned and purified synthesis gas stream from the first train with 0 to 100 volume % of the H.sub.2 -rich gas stream from the first train and at least a portion of the H.sub.2 -rich gas stream from the second train.
    • 一种连续的方法,用于同时生产具有在约2至12范围内的摩尔比H 2 / CO的净化纯化合成气流和富CO气体的单独流。 在该方法的一个实施方案中,生产了清洁和纯化的甲醇合成气和基本上一氧化碳。 可以合成甲醇并任选地与基本上纯的一氧化碳催化反应以产生乙酸。 在本课题中,直接来自自由流未开包的非催化部分氧化合成气发生器的流出气流被分成两股同时在两个分开的列车中处理的物流。 在第一列中,其中一个分流通过气体冷却器中的间接热交换来冷却,然后进一步处理以产生清洁和纯化的合成气流,富H2的气流和富含CO的产物流 气体,优选基本上纯的CO。同时,第二列中的第二分流通过在骤冷鼓中的水中直接淬火来冷却,清洗,进行催化水煤气变换反应,并纯化以产生第二富H2 气流。 然后通过将来自第一列的清洁和纯化的合成气流的至少一部分混合在一起,产生具有在约2至12的范围内的摩尔比H2 / CO的清洁和纯化的合成气的产物流,其中0至100 来自第一列的富H 2气流的体积%和来自第二列的富H2气体流的至少一部分。
    • 146. 发明授权
    • Process for the production of ethylene glycol
    • 生产乙二醇的方法
    • US4087470A
    • 1978-05-02
    • US699099
    • 1976-06-23
    • Shigeto Suzuki
    • Shigeto Suzuki
    • C07C29/149C07C51/10C07C51/12C07C31/18
    • C07C51/10C07C29/149C07C51/12
    • A cyclic process for producing ethylene glycol comprising the steps of:(1) contacting formaldehyde with a synthesis gas comprising carbon monoxide and hydrogen in the presence of a catalytic amount of hydrogen fluoride under conditions effective to deplete carbon monoxide from the synthesis gas and produce glycolic acid and diglycolic acid;(2) contacting the acid product of step (1) with ethylene glycol, diethylene glycol, or mixtures thereof under conditions effective to produce ethylene glycol glycolate and diglycolate, diethylene glycol glycolate and diglycolate, or mixtures thereof;(3) removing residual carbon monoxide from the carbon monoxide depleted synthesis gas of step (1) thereby producing a hydrogen rich gas;(4) contacting the glycolate and diglycolate product of step (2) with the hydrogen-rich gas mixture of step (3) under conditions effective to produce ethylene glycol, diethylene glycol, or mixtures thereof; and(5) recycling from step (4) to step (2) an amount of the glycol product effective to esterify substantially all the acid product present in the reaction zone of step (2).
    • 一种生产乙二醇的循环方法,包括以下步骤: