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METHOD FOR CARBON DIOXIDE GAS CAPTURE FROM SMOKE GAS OF A POWER PLANT AND INSTALLATION FOR ITS IMPLEMENTATION

机译:一种从电厂烟气中捕集二氧化碳的方法及实现方法

摘要

1. A method of collecting carbon dioxide from the flue gas of a power plant, comprising the steps of: 1) providing an organic amine and an ionic liquid in a molar ratio (1-1.1): 1, mixing an organic amine, an ionic liquid and water to obtain an aqueous solution of a composite absorbent, having a concentration of 20-40% by weight; using an aqueous solution of a composite absorbent containing organic amine and an ionic liquid as a CO absorbent, uniformly spraying an aqueous solution of a composite absorbent in flue gas from the rear of the boiler power plants after dust removal and desulfurization, allowing the flue gas to move upward for full contact with the aqueous solution of the composite absorbent sprayed down, and allowing the CO gas to react with the composite absorbent, resulting in CO absorption and a solution rich in A · CO and B · is formed CO, in which A is an organic amine, and B is an ionic liquid; regulation of the liquid-gas ratio from 5 to 25 l / m, the reaction temperature from 40 ° C to 55 ° C, and the reaction pressure from 0.01 to 10 atm (1.01-1013 kPa); 2) allowing the solution to be rich A · CO and B · CO, settle and become transparent under the action of self-aggregation with the formation of various layers of liquid, including the lower layer, which is a mixed solution rich in A · CO and B · CO, and the upper layer, which is an aqueous solution of a composite absorbent; separating the bottom layer to obtain a mixed solution rich in A · CO and B · CO; performing heat exchange on the separated mixed solution rich in A · CO and B · CO to allow CO gas dissolved or absorbed in the aqueous solution of the composite
机译:1.一种从发电厂的烟气中收集二氧化碳的方法,其包括以下步骤:1)以摩尔比(1-1.1)提供有机胺和离子液体:1,混合有机胺,离子液体和水,以获得浓度为20-40%(重量)的复合吸收剂的水溶液;使用包含有机胺和离子液体的复合吸收剂的水溶液作为CO吸收剂,在除尘和脱硫后,从锅炉电厂的后部均匀喷洒复合吸收剂的烟气水溶液,使烟道气向上移动以与喷洒的复合吸收剂的水溶液完全接触,并使CO气体与复合吸收剂反应,导致CO吸收,并形成富含A·CO和B·的溶液,其中CO A是有机胺,B是离子液体;调节液气比为5至25l / m,反应温度为40℃至55℃,反应压力为0.01至10atm(1.01-1013kPa); 2)使溶液富含A·CO和B·CO,在自聚集作用下沉降并变成透明,形成各种液体层,包括下层,这是富含A·CO的混合溶液CO和B·CO,以及上层,其是复合吸收剂的水溶液;分离底层以获得富含A·CO和B·CO的混合溶液。对分离出的富含A·CO和B·CO的混合溶液进行热交换,以使CO气体溶解或吸收到复合材料的水溶液中

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