首页> 外国专利> Production and treatment of synthesis gas, by generating synthesis gas by gasification, where synthesis gas contains hydrogen, carbon monoxide, carbon dioxide, methane, water and impurities and purifying acidic impurities washing in column

Production and treatment of synthesis gas, by generating synthesis gas by gasification, where synthesis gas contains hydrogen, carbon monoxide, carbon dioxide, methane, water and impurities and purifying acidic impurities washing in column

机译:通过气化生成合成气来生产和处理合成气,其中合成气包含氢气,一氧化碳,二氧化碳,甲烷,水和杂质,并纯化塔中洗涤的酸性杂质

摘要

The process comprises generating synthesis gas by gasification, where the synthesis gas contains hydrogen, carbon monoxide, carbon dioxide (CO 2), methane, water and impurities including sulfur compounds, and purifying all or part of the acidic impurities including CO 2and sulfur compounds by washing in a column using an acid gas solvent, where the purification step comprises prewashing a lower part of a gas column to eliminate impurities of hydrogen sulfide and carbonyl sulfide with a fraction of CO 2solvent and to recovery of the lower part of the column of the solvent to CO 2. The process comprises generating synthesis gas by gasification, where the synthesis gas contains hydrogen, carbon monoxide, carbon dioxide (CO 2), methane, water and impurities including sulfur compounds, and purifying all or part of the acidic impurities including CO 2and sulfur compounds by washing in a column using an acid gas solvent, where the purification step comprises prewashing a lower part of a gas column to eliminate impurities of hydrogen sulfide and carbonyl sulfide with a fraction of CO 2solvent and to recovery of the lower part of the column of the solvent to CO 2and sulfur compounds, washing an upper part of the gas column by an acid gas solvent for absorption of CO 2contained in the gas to be purified and for recovery synthesis gas in the upper part of the column and CO 2solvent in the middle of the column, regenerating the solvent produced by a gas expansion at an average pressure and then regenerating the solvent produced by the gas expansion at low pressure of 3 bar, recycling flash gas in the synthesis gas through single recycle compressor after compression, and cryogenic separating the remaining constituents in the synthesis gas with a production of flash gas of the cold box. The flash gas of the cold box is sent in the compressor for recycling the flash gas and the synthesis gas. The purification step is a step of extraction via a physical solvent of type Rectisol(RTM: Acid gas removal process)/ Selexol(RTM: Acid gas removal solvent) using methanol. The cryogenic separating step is immediately preceded by a purification step. All or part of flash gas from the cold box is used as regeneration gas in the purification step before the flash gas sent to the recycle compressor. An independent claim is included for an installation for production and treatment of synthesis gas.
机译:该方法包括通过气化产生合成气,其中合成气包含氢气,一氧化碳,二氧化碳(CO 2),甲烷,水和包括硫化合物的杂质,并通过以下方法纯化全部或部分酸性杂质,包括CO 2和硫化合物使用酸性气体溶剂在塔中洗涤,其中纯化步骤包括预洗涤塔的下部,以用一部分CO 2溶剂除去硫化氢和羰基硫的杂质,并回收塔的下部。溶剂转化为CO 2。该方法包括通过气化生成合成气,其中合成气包含氢气,一氧化碳,二氧化碳(CO 2),甲烷,水和包括硫化合物的杂质,并纯化所有或部分的酸性杂质,包括通过使用酸性气体溶剂在色谱柱中进行洗涤来净化CO 2和含硫化合物,其中纯化步骤包括预洗下部气体c柱以用一部分CO 2溶剂消除硫化氢和羰基硫的杂质,并将溶剂塔的下部回收成CO 2和硫化合物,用酸性气体溶剂洗涤气塔的上部以进行吸收回收要纯化的气体中所含的CO 2并用于回收塔上部的合成气和塔中部的CO 2溶剂,使通过平均压力下的气体膨胀产生的溶剂再生,然后再生通过在3 bar的低压下进行气体膨胀,压缩后通过单个循环压缩机对合成气中的闪蒸气进行再循环,并通过低温分离法分离合成气中的其余成分,从而生产出冷箱的闪蒸气。将冷箱的闪蒸气体送入压缩机,以回收闪蒸气体和合成气。纯化步骤是通过使用甲醇的类型为Rectisol(RTM:酸性气体去除工艺)/ Selexol(RTM:酸性气体去除溶剂)的物理溶剂萃取的步骤。低温分离步骤之前紧接着是纯化步骤。来自冷箱的全部或部分闪蒸气体在送入再循环压缩机之前,在净化步骤中用作再生气体。独立权利要求包括用于生产和处理合成气的设备。

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