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12th International Symposium on District Heating and Cooling

12th International Symposium on District Heating and Cooling

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The <str<strong>on</strong>g>12th</str<strong>on</strong>g> <str<strong>on</strong>g>Internati<strong>on</strong>al</str<strong>on</strong>g> <str<strong>on</strong>g>Symposium</str<strong>on</strong>g> <strong>on</strong> <strong>District</strong> <strong>Heating</strong> <strong>and</strong> <strong>Cooling</strong>,September 5 th to September 7 th , 2010, Tallinn, Est<strong>on</strong>iaSystem 1In the current c<strong>on</strong>figurati<strong>on</strong> of this system 15-20% ofthe energy dem<strong>and</strong> is covered with fuel oil, whichneeds to be reduced. One interesting opti<strong>on</strong> could beto c<strong>on</strong>vert biomass into bio oil by pyrolysis <strong>and</strong> thenuse the bio oil in the existing oil boilers. Bio oil that isnot used within the system can be sold (e.g. summertime). If no pyrolysis reactor is built, a c<strong>on</strong>venti<strong>on</strong>albiofuel fired combined heat <strong>and</strong> power plant (bio CHP)will be invested in, building up the reference case.System 2In this system, there is no need for new producti<strong>on</strong>units, rather there is a high producti<strong>on</strong> capacity,allowing for integrati<strong>on</strong> of a bioenergy producti<strong>on</strong> unit.System 2 has good access to biomass, but might havedifficulties to find a market for large quantities of byproducts.Based <strong>on</strong> these prerequisites, a suitablecombine technology could be cellulose ethanolproducti<strong>on</strong> with enzymatic hydrolysis aiming at highyield <strong>and</strong> in-house use of energy by-products.Regarding the O&M cost for the enzymatic process inTable I, future enzyme price are assumed [4], Withtoday‘s prices, the enzymatic process will not beprofitable.System 3In System 3 there is a need for new producti<strong>on</strong>capacity, which is represented by a bio CHP in thereference case. This system has good access to alarge energy market, which enables output of otherenergy products. Hence, a cellulose ethanol plantbased <strong>on</strong> acid hydrolysis can complement thereference case investment to build up the combinecase.System 4This system is in many aspects similar to System 3, butethanol producti<strong>on</strong> is not in line with company strategy.Moreover, System 3 has good access to peat, whichcould supplement biomass for a large scale producti<strong>on</strong>unit. Hence, gasificati<strong>on</strong> of biomass for producti<strong>on</strong> ofsynthetic biofuel is evaluated for this system.Envir<strong>on</strong>mental evaluati<strong>on</strong>The assessment of the envir<strong>on</strong>mental implicati<strong>on</strong> ofintroducing a bioenergy producti<strong>on</strong> in an existingdistrict heating system focuses <strong>on</strong> changes inemissi<strong>on</strong>s of green house gases (GHG). A systemapproach for analysing the changes of GHG‘s isapplied. This means that besides changes of the directemissi<strong>on</strong>s <strong>on</strong> site, also the changes of emissi<strong>on</strong>s inaffected parts of the energy systems are included; seeFigure 1. For instance, producti<strong>on</strong> of biofuel in thecombines ads to the envir<strong>on</strong>mental benefit since fossilfuels can be replaced, while reduced electricityproducti<strong>on</strong> has a negative impact to the envir<strong>on</strong>mentalbenefit in accordance with marginal electricityproducti<strong>on</strong>.Producti<strong>on</strong>,distributi<strong>on</strong> <strong>and</strong>use of biomassDirect GHG emissi<strong>on</strong>sGHGDH system withor without bioenergyproducti<strong>on</strong>GHGPowersystemProducti<strong>on</strong>,distributi<strong>on</strong> <strong>and</strong> useof transportati<strong>on</strong>fuelGHGFig.1. Illustrati<strong>on</strong> of the applied system approach forassessing the changes of GHG‘s.In the assessment, all GHG‘s of significance areincluded [3]: carb<strong>on</strong> dioxide (CO 2 ), dinitrogen oxide(N 2 O) <strong>and</strong> methane (CH 4 ). For all energy carriers, lifecycle emissi<strong>on</strong>s are c<strong>on</strong>sidered, i.e. both combusti<strong>on</strong>emissi<strong>on</strong>s <strong>and</strong> well-to-gate emissi<strong>on</strong>s such asemissi<strong>on</strong>s from fuel extracti<strong>on</strong>, processing <strong>and</strong>transportati<strong>on</strong>. Also leakages are c<strong>on</strong>sidered whenapplicable. How the GHG‘s for the relevant energycarriers are assessed are described in brief below, amore thorough descripti<strong>on</strong> can be found in [3].Theadopted life cycle GHG emissi<strong>on</strong>s associated withchanges in c<strong>on</strong>sumpti<strong>on</strong>/producti<strong>on</strong> of the energycarriers are summarized in Table II.Table II. Emissi<strong>on</strong> factors for included energy carriers.ENERGY CARRIERBiomass 14-17 1High emissi<strong>on</strong> elec. (E1) 800Low emissi<strong>on</strong> electricity (E2) 260Pyrolysis oil 292Ethanol 307FT diesel 277Fuel oil 312Biogas 207Pellets 286LIFE CYCLE EMISSION(kg CO 2 eq./MWh)1 The lifecycle emissi<strong>on</strong> of biomass is dependent <strong>on</strong> howthe biomass is used in the energy combines (e.g.hydrolysis for fermentati<strong>on</strong> or gasificati<strong>on</strong>)BiomassThe energy input in all four combines is in the form ofbiomass. Producti<strong>on</strong>, distributi<strong>on</strong> <strong>and</strong> use of biomass isrelated to GHG emissi<strong>on</strong>s. The GHG emissi<strong>on</strong> from theuse of biomass differs depending <strong>on</strong> how the biomassis used. Combusti<strong>on</strong> raises emissi<strong>on</strong>s of both methane145

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