脱硫物料衡算

项目编号:项目名称:京能右玉2×300MW机组烟气脱硫工程标题:气相物料平衡表设计条件:设计煤种100%BMCR,一炉一塔，1301717Nm3/hwet,SO22500mg/Nm3(wet,实际O2),124℃日期:2009.9.25版本：6流体序号13471516流体说明原烟气至增压风机原烟气至脱硫塔净烟气出脱硫塔净烟气至烟囱空气至氧化风机氧化空气至脱硫塔烟气流量（干态）Nm3/h12094601215312121531264656465H2O(气态)Nm3/h92257169619169619135135H2O(液态)kg/h0919100烟气流量(湿态)Nm3/h13017171384931138493166006600质量流量kg/h17074001776056177605684368436实际流量Am3/h21652211875255188233482884895SO2kg/h325416316300SO3kg/h65464600O2vol.%5.635.675.672121相对于标准CO2vol.%12.1412.1812.180.030.03干态、实际SO2mg/Nm3269113413400氧含量下SO3mg/Nm354373700HCL(CL)mg/Nm3869900HF(F)mg/Nm3273300烟尘mg/Nm3108545400SO2at6%O2mg/Nm32626131131SOxasSO2at6%O2mg/Nm32668160160SO3at6%O2mg/Nm3533737HClat6%O2mg/Nm38488HFat6%O2mg/Nm32633烟尘at6%O2mg/Nm31055252压力mbar8868778748661766温度°C12447472080项目编号:项目名称:京能右玉2×300MW机组烟气脱硫工程标题:设计条件:设计煤种100%BMCR,一炉一塔，1301717Nm3/hwet,SO22500mg/Nm3(wet,实际O2),124℃日期:2009.9.25版本：6流体序号20223132333435363739流体说明石灰石到石灰石贮仓石灰石浆液去吸收塔吸收塔石膏浆液去脱水系统石膏浆液去真空皮带脱水机石膏旋流器顶流石膏副产品真空皮带脱水机滤液去制浆系统石膏旋流器顶流返回吸收塔石膏旋流器顶流去废水旋流器废水旋流器底流返回吸收塔质量流量kg/h564417777689561760651350965604355877921732体积流量m³/h5.6414.2262.4812.5249.969.660.0042.387.581.62水流量（含溶解盐）kg/h0124445861388034981096604225275581558固体流量kg/h564453331034388031541869101307234173石膏kg/h00919484067898299066912093亚硫酸钙kg/h0021192190200CaCO3kg/h507950792611491121470951711MgCO3kg/h1411414828212701832CaF2kg/h0013121110100MgF2kg/h0040373360310烟尘kg/h00280562245501903424惰性物质kg/h113113486973899603305942其它kg/h310000000000可溶物kg/h051554233132100112020041氯含量ppm010016370163701637000163701637016370密度kg/m³1000125011041406102810001015102810281071固体含量%100%30%15%50%3.0%90%0.83%3.0%3.0%10%温度°C20204747474747474747液相和悬浮物物料平衡表项目编号:项目名称:京能右玉2×300MW机组烟气脱硫工程标题:设计条件:设计煤种100%BMCR,一炉一塔，1301717Nm3/hwet,SO22500mg/Nm3(wet,实际O2),124℃日期:2009.9.25版本：6流体序号40455556596063677884流体说明废水旋流站顶流至废水处理系统废水旋流器顶流真空皮带脱水机滤液真空皮带脱水机滤布冲洗水真空皮带脱水机滤液返回吸收塔FGD工艺水工艺水去制浆系统工艺水至除雾器冲洗电厂补充水至真空泵密封真空泵密封水至脱水机滤布冲洗质量流量kg/h606160611345056121345070849124445290555005500体积流量m³/h5.965.9613.255.4913.2570.8512.4452.905.505.50水流量（含溶解盐）kg/h600060001333755001333770849124445290555005500固体流量kg/h616111211211205000石膏kg/h272710710710700000亚硫酸钙kg/h0000000000CaCO3kg/h6622200000MgCO3kg/h1100000000CaF2kg/h0000000000MgF2kg/h0000000000烟尘kg/h101011100000惰性物质kg/h171711100000其它kg/h0000000000可溶物kg/h159159236282362852122氯含量ppm163701637010906312110906100100100100100密度kg/m³1016101610151022101510001000100010001000固体含量%1.0%1.0%0.8%2.0%0.8%0.0%0%0.0%0%0%温度°C47474747472525252525液相和悬浮物物料平衡表（续）项目编号:项目名称:京能右玉2×300MW机组烟气脱硫工程标题:气相物料平衡表设计条件:设计煤种100%BMCR,一炉一塔，1301717Nm3/hwet,SO23125mg/Nm3(+25%,wet,实际O2),124℃日期:2009.9.25版本：6流体序号13471516流体说明原烟气至增压风机原烟气至脱硫塔净烟气出脱硫塔净烟气至烟囱空气至氧化风机氧化空气至脱硫塔烟气流量（干态）Nm3/h12094601215209121520964656465H2O(气态)Nm3/h92257170985170985135135H2O(液态)kg/h0919100烟气流量(湿态)Nm3/h13017171386194138619466006600质量流量kg/h17078671777277177727784368436实际流量Am3/h21652211877816188492482884895SO2kg/h406836636600SO3kg/h65464600O2vol.%5.635.665.662121相对于标准CO2vol.%12.1412.1912.190.030.03干态、实际SO2mg/Nm3336330130100氧含量下SO3mg/Nm354373700HCL(CL)mg/Nm3869900HF(F)mg/Nm3273300烟尘mg/Nm3108545400SO2at6%O2mg/Nm33282295295SOxasSO2at6%O2mg/Nm33324324324SO3at6%O2mg/Nm3533737HClat6%O2mg/Nm38488HFat6%O2mg/Nm32633烟尘at6%O2mg/Nm31055252压力mbar8868778748661766温度°C12447472080项目编号:项目名称:京能右玉2×300MW机组烟气脱硫工程标题:设计条件:设计煤种100%BMCR,一炉一塔，1301717Nm3/hwet,SO23125mg/Nm3(+25%,wet,实际O2),124℃日期:2009.9.25版本：6流体序号20223132333435363739流体说明石灰石到石灰石贮仓石灰石浆液去吸收塔吸收塔石膏浆液去脱水系统石膏浆液去真空皮带脱水机石膏旋流器顶流石膏副产品真空皮带脱水机滤液去制浆系统石膏旋流器顶流返回吸收塔石膏旋流器顶流去废水旋流器废水旋流器底流返回吸收塔质量流量kg/h6708211298238621035613521153905355977921732体积流量m³/h6.7116.9174.7014.9759.7311.540.0052.157.591.62水流量（含溶解盐）kg/h014790700281051759511115405195375581558固体流量kg/h67086339123581051718411038501607234173石膏kg/h0011031100599729933084812395亚硫酸钙kg/h0025232220200CaCO3kg/h6037603731217813417601171711MgCO3kg/h1681685833253202232CaF2kg/h0013121110100MgF2kg/h0040374360300烟尘kg/h00287572305702012921惰性物质kg/h13413459211847411704146043其它kg/h369000000000可溶物kg/h061818273154500134919640氯含量ppm010016397163971639700163971639716397密度kg/m³1000124911031405102710001014102710271070固体含量%100%30%15%50%3.0%90%0.83%3.0%3.0%10%温度°C20204747474747474747液相和悬浮物物料平衡表项目编号:项目名称:京能右玉2×300MW机组烟气脱硫工程标题:设计条件:设计煤种100%BMCR,一炉一塔，1301717Nm3/hwet,SO23125mg/Nm3(+25%,wet,实际O2),124℃日期:2009.9.25版本：6流体序号40455556596063677884流体说明废水旋流站顶流至废水处理系统废水旋流器顶流真空皮带脱水机滤液真空皮带脱水机滤布冲洗水真空皮带脱水机滤液返回吸收塔FGD工艺水工艺水去制浆系统工艺水至除雾器冲洗电厂补充水至真空泵密封真空泵密封水至脱水机滤布冲洗质量流量kg/h606160611599666331599672481147905119165006500体积流量m³/h5.975.9715.776.4915.7772.4814.7951.196.506.50水流量（含溶解盐）kg/h600060001586465001586472481147905119165006500固体流量kg/h616113313313306000石膏kg/h282812712712700000亚硫酸钙kg/h0000000000CaCO3kg/h6622200000MgCO3kg/h1100000000CaF2kg/h0000000000MgF2kg/h0000000000烟尘kg/h8811100000惰性物质kg/h171711100000其它kg/h0000000000可溶物kg/h156156276332762962033氯含量ppm163971639710974316310974100100100100100密度kg/m³1015101510141021101410001000100010001000固体含量%1.0%1.0%0.8%2.0%0.8%0.0%0%0.0%0%0%温度°C47474747472525252525液相和悬浮物物料平衡表（续）项目编号:项目名称:京能右玉2×300MW机组烟气脱硫工程标题:气相物料平衡表设计条件:校核煤种100%BMCR,一炉一塔，1157616Nm3/hwet,SO22000mg/Nm3(wet,实际O2),