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Adding gas from biomass to the gas grid - SGC

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4.3.4 Upgrading by absorption of carbon dioxide without chemical reactionRemoval of carbon dioxide by water wash with regenerationCarbon dioxide can be absorbed in a physical absorption process. The carbon dioxide is dissolvedin <strong>the</strong> absorbent without any chemical reaction taking place. Regeneration of <strong>the</strong> solvent is madeei<strong>the</strong>r by flashing (decreased pressure), by heating a combination of both. Water is <strong>the</strong> mostcommonly used solvent for absorbing carbon dioxide <strong>from</strong> bio<strong>gas</strong>. The solubility for carbon dioxidein water increases with increasing pressure. Water can ei<strong>the</strong>r be regenerated and reused forabsorption in a circulation system or used for absorption in a single pass flow.Carbon dioxide is absorbed in water at elevated pressure. Cleaned bio<strong>gas</strong> is compressed and fedin<strong>to</strong> <strong>the</strong> bot<strong>to</strong>m of an absorption column. Water is fed <strong>from</strong> <strong>the</strong> <strong>to</strong>p of <strong>the</strong> column <strong>to</strong> achieve a <strong>gas</strong>liquidcounter flow. The column is equipped with random packing <strong>to</strong> give a large surface for <strong>gas</strong>liquidcontact and internals for <strong>the</strong> collecting and redistribution of water. Carbon dioxide is absorbedby <strong>the</strong> water and <strong>the</strong> <strong>gas</strong> leaving <strong>the</strong> <strong>to</strong>p of <strong>the</strong> column is stripped <strong>from</strong> most of <strong>the</strong> carbon dioxidecontent.Methane is partly soluble in pressurised water and <strong>the</strong>refore some methane will be removed with<strong>the</strong> water. To minimise <strong>the</strong> losses of methane, <strong>the</strong> water is depressurised in a flash tank afterleaving <strong>the</strong> absorption column. The released <strong>gas</strong> mixture is rich in methane and is recirculated <strong>to</strong><strong>the</strong> compressor inlet.Water <strong>from</strong> <strong>the</strong> flash tank is depressurised <strong>to</strong> atmospheric pressure and fed in<strong>to</strong> <strong>the</strong> <strong>to</strong>p of adesorption column. Air is blown <strong>from</strong> <strong>the</strong> bot<strong>to</strong>m of <strong>the</strong> desorption column <strong>to</strong> remove dissolvedcarbon dioxide <strong>from</strong> <strong>the</strong> water. The desorption column is equipped with internals and packing in <strong>the</strong>same way as <strong>the</strong> absorption column. The regenerated liquid is cooled in a heat exchanger <strong>to</strong>maintain <strong>the</strong> absorption temperature and recycled <strong>to</strong> <strong>the</strong> absorption column.The vent <strong>gas</strong> is ei<strong>the</strong>r released <strong>to</strong> <strong>the</strong> atmosphere or treated in some kind of <strong>gas</strong> filter <strong>to</strong> removeodours.Hydrogen sulphide is absorbed <strong>to</strong>ge<strong>the</strong>r with carbon dioxide in <strong>the</strong> absorption column. The solubilityfor hydrogen sulphide in water is ra<strong>the</strong>r high and all hydrogen sulphide cannot be removed in <strong>the</strong>desorption column. Fur<strong>the</strong>rmore, part of <strong>the</strong> hydrogen sulphide is oxidised with air <strong>to</strong> elementarysulphur in <strong>the</strong> desorption column. This sulphur is accumulated in <strong>the</strong> system and can causeproblems with plugging and fouling after some period of operation. It is <strong>the</strong>refore desirable that highcontents of hydrogen sulphide are removed before <strong>the</strong> absorption. The product <strong>gas</strong> is saturated withwater and has <strong>to</strong> be dried.page: 38

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