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当前位置:首页 > 商业/管理/HR > 项目/工程管理 > 寒区沼气发酵地源热泵增温系统的初步研究陈泽兴
150030、。33h。。S216.2A1003-188X201103-0219-040、。。±2℃。±1.5~2℃1。±3℃±5℃2。。、、。11.11。、32010-04-27GA09B503-11985-E-mailze_xing_chen@163.com。1965-E-mailliujy@neau.edu.cn。。、、。。、、、。。、、。。1.2。。、。。235±2℃。700m3630m3。30m3230m3。2.1QL0℃·912·201133DOI:10.13427/j.cnki.njyi.2011.03.0260℃35℃。QLQL=ρVCΔt1ρ1000kg/m3VV=30m3/dC4.2kJ/kg·℃3ΔtΔt=35℃。1QL=51kW。1.2.3.4.5.6.7.8.9.10.11.12.13.14.1Fig.1Thechartofgroundwater-sourceheatpumpheatingsystem2.2QF2。2Fig.2Thestructureofanaerobicfermentationreactor。δ51mm。QF1QF1=Htw-ff÷12πλ1lnd1+2δ1d1+12πλ2lnd1+2δ1+δ2d1+2δ1+1hfπd1+2δ1+δ2{}2HH=6mtwtw=35℃tftf=-23℃4λ12.05W/m·K5λ20.047W/m·K6hf23.2W/m·K7d1d1=12.22mδ1δ1=8mmδ2δ2=150mm。2QF1=4.179kW。QF2QF2=tw-tTδ3λ3+δ4λ4·πd2143tT0.6m-4℃8δ3C30δ3=500mmδ4C15δ4=100mmλ3C301.51W/m·Kλ4C151.28W/m·K4。3QF2=11.20kW。QF=QF1+QF2=15.379kW。Q=QL+QF·022·201133=66.379kW。1LSH65S72kW。3201012421-2010126633h1。1Tab.1Testdateofgroundvater-sourceheatfumpheatingsystem/℃/℃/m3·h-1/℃/℃/W/℃/℃2010012421002200230024005555222210.810.810.810.8373737373434343410663.410797.611027.110985.834.534.534.534.5-14-13-13-920100125100200300400500600700800110012001400150016001700200022002300555555555554555552222222222222222210.810.810.810.810.810.810.810.810.810.810.810.810.810.810.810.810.83737373737373737383837373738383838343434343434343434343434343434343410944.511163.510971.010971.010903.210891.511029.010934.4104049805.68547.09419.210342.48340.88972.68793.510547.234.534.534.534.534.534.534.534.534.534.534.534.534.534.534.534.534.5-9-9-9.5-9.8-11.1-12-13-13-12-11.5-13-14.5-16-17-17-18-242010012610020030040050060055545522222210.810.810.810.810.810.83737383838383435353535359439.2952286528776.89165.38777.634.534.534.534.534.534.5-23-27-25-27-26-254.93210.837.3734.1910029.234.5-15.98Qd=VdρdCdΔtd=36.8kWVdVd=10.8m3/hρdρd=1000kg/m3CdCd=4.2kJ/kg·℃Δtd。10.0kW0.757.5kWQh=44.3kW。33h5262840kJ。ε=44.37.5=5.91-9~-27℃38℃35±0.5℃。·122·20113344.19ε=5.9。QdQh=0.830783.1%16.9%。4.21188000kJ。Brby=11880007000×4.1868η1η2=150kg。η1η1=0.3η2η2=0.970001kgkcal4.18681kcal=4.1868kJ。33hB=52628407000×4.1868η'1η'2=270kgη'1η'1=0.7η'2η2=0.95。33hΔB=B-Brby=120kgΔBB=120270=44.44%535±0.5℃。44%。1.M.2004.2.M.2008115-116.3.J.200927334-3539.4.K.1987.5.EB/OL.2010-01-04.http//.naimo.cn.6.M.2008.7.M.1994.8.Z.1973.9.J.19989141-42.PreliminaryStudyofOperationParametersforGroundHeatPumpHeatingSystemofBiogasFermentationinAlpineRegionChenZexingLiuJianyuLiWentaoCollegeofEngineeringNortheastAgricultureUniversityHarbin150030ChinaAbstractThisresearchwastostudytheheatingsystemoflarge-scalebiogasprojectinLanlingvillageJixiHei-longjiangProvince.Accordingtotheheatemissioncalculationofmixingpoolandanaerobicfermentationreactortheheat-ingloadofheatingsystemwasidentifiedandthegroundwater-sourceheatpumpwasmatched.33-hourperiodtestandcorrespondinganalysisofheatingsystemwasconducted.Thetestresultspointedoutthattheheatingsystemgroundwater-sourceheatpumpsystemofbiogasprojectcanmakesurethatthebiogasprojectrunwellincoldwinterandhighener-gyefficiencyofheatingsystemwaswellreflected.Keywordsgroundwater-sourceheatpumpbiogasanaerobicfermentationheatingload·222·201133
本文标题:寒区沼气发酵地源热泵增温系统的初步研究陈泽兴
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