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Adding gas from biomass to the gas grid - SGC

Adding gas from biomass to the gas grid - SGC

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Parameter Unit Process Plant exampleLocation/nameLaholmCapacity range M 3 bio<strong>gas</strong>/h 100 <strong>to</strong> > 10,000 250Input· methane%45 - 7569 - 72· carbon dioxide %25 - 5528 - 31· nitrogen%< 10 - 0.2· hydrogen sulphideppm< 10 10 0 - 15Output· methane· carbon dioxide· air· dewpoint· hydrogen sulphideProcess conditionsAbsorption pressureAbsorption temperaturePressure in flash tankDesorption pressureSelexol flowSupplier%%%°CppmBar°Cbarmbar (abs)m 3 /h> 98< 2< 1.5< -20095 - 982 - 50 - 0.5< -60010 - 127 - 920 - 3572 - 51.5 - 2atmospheric <strong>to</strong> 2009503 - 6 11 10 - 15Malmberg Water ABTable 15: Removal of carbon dioxide using Selexol4.3.5 Removal of carbon dioxide by chemical reactionThis process is based on <strong>the</strong> same principle as <strong>the</strong> absorption processes without chemical reaction,see § 4.3.4. The raw <strong>gas</strong> is led through a liquid, typically at elevated pressure and temperature, and<strong>the</strong> undesired components (e.g. CO 2 , H 2 S) are absorbed in <strong>the</strong> liquid. However, instead of simplydissolving <strong>the</strong>se components, <strong>the</strong> liquid reacts chemically with <strong>the</strong>m and <strong>the</strong>refore drives <strong>the</strong>m in<strong>to</strong>solution.Due <strong>to</strong> absorber costs and <strong>the</strong> disposal of contaminated absorber, <strong>the</strong> absorber is alwaysregenerated, i.e. single pass operation know, <strong>from</strong> water scrubbers are not applied. The process iscontinuous and <strong>the</strong> absorber is regenerated in a reversal chemical reaction in which <strong>the</strong> absorbedCO 2 is released.Table 15 illustrates <strong>the</strong> characteristics of a number of <strong>gas</strong> treatment processes with absorption inchemically reacting absorbers. The alkanolamines MEA, DEA and DGA are examples of absorbers.Several of <strong>the</strong> alkanolamines also absorb a significant amount of <strong>the</strong> water contained in <strong>the</strong> bio<strong>gas</strong>.MEA, that is an organic base in an aqueous solution, is one of <strong>the</strong> most feasible chemicalabsorbers. MEA is often used in <strong>gas</strong> separation processes in e.g. CO 2 production <strong>from</strong> flue <strong>gas</strong>es,cleaning of natural <strong>gas</strong>es, and production of hydrogen and ammonia. It is a colourless, viscous,1011Excess H 2S (> 10 ppm) removed separately <strong>to</strong> reduce energy costsDepending on <strong>the</strong> absorption pressure, for every 100 m 3 /h processed bio<strong>gas</strong>page: 43

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