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    • 1. 发明授权
    • Process for the preparation of ethanol and higher alcohols
    • 乙醇和高级醇的制备方法
    • US08637580B2
    • 2014-01-28
    • US13808240
    • 2011-05-17
    • Poul Erik Højlund NielsenBurcin TemelPablo Beato
    • Poul Erik Højlund NielsenBurcin TemelPablo Beato
    • C07C27/00
    • C07C29/1516C07C29/1512C07C29/32C07C31/08C07C31/10C07C31/12C07C31/125
    • Process for the preparation of ethanol and/or higher alcohols comprising the steps of: (a) providing an alcohol synthesis gas comprising carbon monoxide and hydrogen in a molar ratio of higher than 0.5; (c) adding an amount of methanol and/or higher alcohols to the synthesis gas to obtain a synthesis gas mixture. (d) converting the synthesis gas mixture from step (c) in presence of one or more catalysts catalysing the conversion of the synthesis gas mixture into a ethanol and/or higher alcohols containing product; and (e) withdrawing the product from step (d), wherein the synthesis gas is purified by removing iron and nickel carbonyl compounds prior or after the addition methanol and/or higher alcohols to the synthesis gas and optionally (I) cooling the withdrawn product in step (e); and (g) contacting the cooled product with a hydrogenation catalyst.
    • 制备乙醇和/或高级醇的方法包括以下步骤:(a)提供摩尔比高于0.5的一氧化碳和氢气的醇合成气; (c)向合成气中加入一定量的甲醇和/或高级醇以得到合成气体混合物。 (d)在催化合成气混合物转化为乙醇和/或高级醇的产物的一种或多种催化剂的存在下,转化来自步骤(c)的合成气混合物; 和(e)从步骤(d)中取出产物,其中通过在向合成气中加入甲醇和/或高级醇之前或之后除去铁和镍羰基化合物来纯化合成气,并且任选地(I)冷却所提取的产物 在步骤(e)中; 和(g)使冷却的产物与氢化催化剂接触。
    • 3. 发明申请
    • PROCESS FOR THE PREPARATION OF ETHANOL AND HIGHER ALCOHOLS
    • 制备乙醇和高级醇的方法
    • US20130123377A1
    • 2013-05-16
    • US13808240
    • 2011-05-17
    • Poul Erik Højlund NielsenBurcin TemelPablo Beato
    • Poul Erik Højlund NielsenBurcin TemelPablo Beato
    • C07C29/151
    • C07C29/1516C07C29/1512C07C29/32C07C31/08C07C31/10C07C31/12C07C31/125
    • Process for the preparation of ethanol and/or higher alcohols comprising the steps of: (a) providing an alcohol synthesis gas comprising carbon monoxide and hydrogen in a molar ratio of higher than 0.5; (c) adding an amount of methanol and/or higher alcohols to the synthesis gas to obtain a synthesis gas mixture. (d) converting the synthesis gas mixture from step (c) in presence of one or more catalysts catalysing the conversion of the synthesis gas mixture into a ethanol and/or higher alcohols containing product; and (e) withdrawing the product from step (d), wherein the synthesis gas is purified by removing iron and nickel carbonyl compounds prior or after the addition methanol and/or higher alcohols to the synthesis gas and optionally (I) cooling the withdrawn product in step (e); and (g) contacting the cooled product with a hydrogenation catalyst.
    • 制备乙醇和/或高级醇的方法包括以下步骤:(a)提供摩尔比高于0.5的一氧化碳和氢气的醇合成气; (c)向合成气中加入一定量的甲醇和/或高级醇以得到合成气体混合物。 (d)在催化合成气混合物转化为乙醇和/或高级醇的产物的一种或多种催化剂的存在下,转化来自步骤(c)的合成气混合物; 和(e)从步骤(d)中取出产物,其中通过在向合成气中加入甲醇和/或高级醇之前或之后除去铁和镍羰基化合物来纯化合成气,并且任选地(I)冷却所提取的产物 在步骤(e)中; 和(g)使冷却的产物与氢化催化剂接触。
    • 9. 发明授权
    • Process for the preparation of synthesis gas from black liquor
    • 从黑液制备合成气的方法
    • US08038906B2
    • 2011-10-18
    • US12431240
    • 2009-04-28
    • Poul Erik Højlund NielsenBodil Voss
    • Poul Erik Højlund NielsenBodil Voss
    • D21C11/00C10J3/46C01B3/24
    • C01B3/36C01B3/32C01B3/50C01B3/52C01B2203/0415C01B2203/047C01B2203/0475C07C41/01D21C11/125C07C43/043
    • A process for the adjustment of the composition of a synthesis gas produced in a high temperature black liquor gasifier. The process includes the steps of (a) generating a gasifier effluent stream from black liquor in the gasifier by a blast and optionally an atomising stream; (b) optionally quenching the gasifier effluent stream with a gas stream to form a gas quenched effluent stream; (c) quenching the gasifier effluent of step (a) or the gas quenched effluent gas stream of step (b) with a water stream to form a raw synthesis gas; (d) further cooling and cleaning and separating the raw synthesis gas to form a purified unprocessed synthesis gas with an appropriate H2/CO ratio; (e) partly converting the purified synthesis gas to dimethyl ether in a synthesis section, producing at least a product stream of DME and a hydrogen rich purge stream of processed; (f) splitting and recycling individual or combinations of split streams of the processed or the unprocessed synthesis gas to step a and/or step (b); and recycling a by-product stream of CO2 being further generated in step (e) in part or completely to step (a) and/or step (b).
    • 用于调节在高温黑液气化器中生产的合成气的组成的方法。 该方法包括以下步骤:(a)通过鼓风和任选的雾化流从气化器中的黑液生成气化器流出物流; (b)任选地用气流骤冷气化器流出物流以形成气体骤冷流出物流; (c)用水流淬火步骤(a)的气化器流出物或步骤(b)的气体骤冷流出物气流,以形成原始合成气; (d)进一步冷却和清洗并分离原始合成气以形成具有合适H 2 / CO比的纯化未加工合成气; (e)在合成部分中部分地将纯化的合成气转化为二甲醚,至少产生DME的产物流和加氢的富氢吹扫流; (f)将经处理或未经处理的合成气的分流或分离流分离和回收到步骤a和/或步骤(b); 并且在步骤(e)中再次产生副产物二氧化碳流,部分或完全是步骤(a)和/或步骤(b)。