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疏水放流式1红色汇集式0黑色汽轮机排汽焓hn2346.8凝结水焓tn136.3轴封加热器轴封加热器出口焓140.98段抽汽焓h124898#低加出口焓t12437段抽汽焓h22606.57#低加出口焓t2327.96段抽汽焓h32741.46#低加出口焓t3422.65段抽汽焓h42948.95#低加出口焓t4565.4除氧器出口焓t5718.2给水泵出口焓t5'743.33段抽汽焓h63362.53#高加出口焓t6880.42段抽汽焓h73017.42#高加出口焓t71042再热蒸汽焓h7'3539.9--1段抽汽焓h831331#高加出口焓t81196新蒸汽焓h93396.9---新蒸汽量kg/h900671---所占新蒸汽比例比焓高压缸密封损失汽量kg/h108.8αf10.00012高压缸密封流入低压缸汽封7440.00083高压缸密封损失进入低压缸汽量8784.90.00975高压缸流入中压缸kg/h89570.00994高压缸流入再热冷段kg/h83200.00924主阀汽封损失kg/h116.10.00013主阀汽封至3#高加419.60.00047中压缸密封损失汽量kg/h102.6αf20.00011中压缸密封进入低压缸汽封7020.00078汽封进入凝汽器7400.00082低压缸密封损失汽量3300.00037供热抽汽kg/h00工业抽汽kg/h00给水泵耗气量kg/h31911αf30.03543供热抽汽凝水温度℃45凝水回水位置凝汽器热井8#低加凝结水焓升τ1102.18段抽汽蒸汽释放热量q12324.77#低加凝结水焓升τ284.97段抽汽蒸汽释放热量q22341.56#低加凝结水焓升τ394.76段抽汽蒸汽释放热量q32391.45#低加凝结水焓升τ4142.85段抽汽蒸汽释放热量q42503.9除氧器给水焓升τ5152.84段抽汽蒸汽释放热量q52583.93#高加给水焓升τ6137.13段抽汽蒸汽释放热量q62605计算结果说明加热器型式基础参数（根据汽轮机热平衡图，输入下列数据）4段抽汽焓h53149.3其他抽汽参数2#高加给水焓升τ7161.62段抽汽蒸汽释放热量q721191#高加给水焓升τ81541段抽汽蒸汽释放热量q82066.7低压缸排汽率αn0.6115572---供热抽汽凝结水率α1n08段抽汽率α10.02979978段抽汽焓降H1142.27段抽汽率α20.02547327段抽汽焓降H2253.546段抽汽率α30.02896566段抽汽焓降H3379.2365段抽汽率α40.04424675段抽汽焓降H4571.671低压缸进汽率αH0.7400424---4段抽汽率α50.04503464段抽汽焓降H5739.4413段抽汽率α60.04479363段抽汽焓降H6897.6672段抽汽率α70.07035822段抽汽变热量焓降H71026.51---2段抽汽定热量焓降H7'788.9641段抽汽率α80.07451491段抽汽变热量焓降H81060.78---1段抽汽定热量焓降H8'842.05新蒸汽焓降kJ/kg1198.9输出功299949高压缸做功新蒸汽吸热量kJ/kg2637.0中压缸做功机组热效率-0.45464低压缸做功0.4548039输出功合计数据名称深绿色计算得出原始数据凝水泵出口焓138.5轴封加热器疏水焓415轴封加热器18#低加疏水焓ts1164.38#低加17#低加疏水焓ts22657#低加16#低加疏水焓ts33506#低加15#低加疏水焓ts44455#低加1除氧器疏水焓ts5727除氧器0给水泵功耗τb25.1--3#高加疏水焓ts6757.53#高加12#高加疏水焓ts7898.42#高加1--1#高加疏水焓ts81066.31#高加10-------8#疏水释放热量γ1100.77#疏水释放热量γ2856#疏水释放热量γ3955#疏水释放热量γ404#疏水释放热量γ5192.13#疏水释放热量γ6140.9计算结果说明基础参数（根据汽轮机热平衡图，输入下列数据）加热器型式过程参数，为零过程参数，为零2#疏水释放热量γ7167.91#疏水释放热量γ80---8段抽汽做功效率η10.06117低压缸排汽量550811.97段抽汽做功效率η20.108288段抽汽量26839.76段抽汽做功效率η30.158587段抽汽量22943.05段抽汽做功效率η40.228316段抽汽量26088.4---5段抽汽量39851.84段抽汽做功效率η50.28617低压缸进汽量666534.73段抽汽做功效率η60.344594段抽汽量40561.42段抽汽变热量效率η70.484433段抽汽量40344.32段抽汽定热量效率η7'0.372332段抽汽量63369.61段抽汽变热量效率η80.513271段抽汽定热量效率η8'0.403031段抽汽量67113.490912.9kW88826.2kW119792.8kW299531.9kW疏水放流式1红色汇集式0黑色汽轮机排汽焓hn2346.8凝结水焓tn136.3轴封加热器轴封加热器出口焓140.98段抽汽焓h124898#低加出口焓t12437段抽汽焓h22606.57#低加出口焓t2327.96段抽汽焓h32741.46#低加出口焓t3422.65段抽汽焓h42948.95#低加出口焓t4565.4除氧器出口焓t5718.2给水泵出口焓t5'743.33段抽汽焓h63362.53#高加出口焓t6880.42段抽汽焓h73017.42#高加出口焓t71042再热蒸汽焓h7'3539.9--1段抽汽焓h831331#高加出口焓t81196新蒸汽焓h93396.9---新蒸汽量kg/h900671---所占新蒸汽比例比焓高压缸密封损失汽量kg/h108.8αf10.00012高压缸密封流入低压缸汽封7440.00083高压缸密封损失进入低压缸汽量8784.90.00975高压缸流入中压缸kg/h89570.00994高压缸流入再热冷段kg/h83200.00924主阀汽封损失kg/h116.10.00013主阀汽封至3#高加419.60.00047中压缸密封损失汽量kg/h102.6αf20.00011中压缸密封进入低压缸汽封7020.00078汽封进入凝汽器7400.00082低压缸密封损失汽量3300.00037供热抽汽kg/h3000000.33308工业抽汽kg/h00给水泵耗气量kg/h31911αf30.03543供热抽汽凝水温度℃45凝水回水位置凝汽器热井8#低加凝结水焓升τ1102.18段抽汽蒸汽释放热量q12324.77#低加凝结水焓升τ284.97段抽汽蒸汽释放热量q22341.56#低加凝结水焓升τ394.76段抽汽蒸汽释放热量q32391.45#低加凝结水焓升τ4142.85段抽汽蒸汽释放热量q42503.9除氧器给水焓升τ5152.84段抽汽蒸汽释放热量q52583.93#高加给水焓升τ6137.13段抽汽蒸汽释放热量q62605其他抽汽参数计算结果说明加热器型式基础参数（根据汽轮机热平衡图，输入下列数据）4段抽汽焓h53149.32#高加给水焓升τ7161.62段抽汽蒸汽释放热量q721191#高加给水焓升τ81541段抽汽蒸汽释放热量q82066.7低压缸排汽率αn0.2784722---供热抽汽凝结水率α1n0.3330858段抽汽率α10.02979978段抽汽焓降H1142.27段抽汽率α20.02547327段抽汽焓降H2253.546段抽汽率α30.02896566段抽汽焓降H3379.2365段抽汽率α40.04424675段抽汽焓降H4571.671低压缸进汽率αH0.4069574---4段抽汽率α50.04503464段抽汽焓降H5739.4413段抽汽率α60.04479363段抽汽焓降H6897.6672段抽汽率α70.07035822段抽汽变热量焓降H71026.51---2段抽汽定热量焓降H7'841.9271段抽汽率α80.07451491段抽汽变热量焓降H81060.78---1段抽汽定热量焓降H8'890.817新蒸汽焓降kJ/kg931.6输出功233074高压缸做功新蒸汽吸热量kJ/kg2637.0中压缸做功机组热效率-0.353276低压缸做功输出功合计供热输出热量数据名称深绿色计算得出原始数据凝水泵出口焓138.5轴封加热器疏水焓415轴封加热器18#低加疏水焓ts1164.38#低加17#低加疏水焓ts22657#低加16#低加疏水焓ts33506#低加15#低加疏水焓ts44455#低加1除氧器疏水焓ts5727除氧器0给水泵功耗τb25.1--3#高加疏水焓ts6757.53#高加12#高加疏水焓ts7898.42#高加1--1#高加疏水焓ts81066.31#高加10-------8#疏水释放热量γ1100.77#疏水释放热量γ2856#疏水释放热量γ3955#疏水释放热量γ404#疏水释放热量γ5192.13#疏水释放热量γ6140.9过程参数，为零过程参数，为零计算结果说明基础参数（根据汽轮机热平衡图，输入下列数据）加热器型式2#疏水释放热量γ7167.91#疏水释放热量γ80---8段抽汽做功效率η10.06117低压缸排汽量250811.97段抽汽做功效率η20.108288段抽汽量26839.76段抽汽做功效率η30.158587段抽汽量22943.05段抽汽做功效率η40.228316段抽汽量26088.4---5段抽汽量39851.84段抽汽做功效率η50.28617低压缸进汽量366534.73段抽汽做功效率η60.344594段抽汽量40561.42段抽汽变热量效率η70.484433段抽汽量40344.32段抽汽定热量效率η7'0.397322段抽汽量63369.61段抽汽变热量效率η80.513271段抽汽定热量效率η8'0.403031段抽汽量67113.490912.9kW88826.2kW52917.8kW232656.9kW246744.2kW疏水放流式1红色汇集式0黑色汽轮机排汽焓hn2370.5凝结水焓tn136.3轴封加热器轴封加热器出口焓141.68段抽汽焓h12496.78#低加出口焓t1218.57段抽汽焓h22612.67#低加出口焓t2298.96段抽汽焓h32747.76#低加出口焓t3388.85段抽汽焓h42957.75#低加出口焓t4525除氧器出口焓t5667.9给水泵出口焓t5'692.83段抽汽焓h63370.73#高加出口焓t6819.42段抽汽焓h73010.62#高加出口焓t7967.1再热蒸汽焓h7'3547.9--1段抽汽焓h831231#高加出口焓t81104.3新蒸汽焓h93417---新蒸汽量kg/h652189---所占新蒸汽比例比焓高压缸密封损失汽量kg/h109.1αf10.00017高压缸密封流入低压缸汽封531.60.00082高压缸密封损失进入低压缸汽量6525.50.01001高压缸流入中压缸kg/h89570.01373高压缸流入再热冷段kg/h83200.01276主阀汽封损失kg/h116.10.00018主阀汽封至3#高加419.60.00064中压缸密封损失汽量kg/h102.6αf20.00016中压缸密封进入低压缸汽封7020.00108汽封进入凝汽器7400.00113低压缸密封损失汽量3300.00051供热抽汽kg/h3000000.45999工业抽汽kg/h00给水泵耗气量kg/h31911αf30.04893供热抽汽凝水温度℃45凝水回水位置凝汽器热井8#低加凝结水焓升τ176.98段抽汽蒸汽释放热量q12331.77#低加凝结水焓升τ280.47段抽汽蒸汽释放热量q22372.26#低加凝结水焓升τ389.96段抽汽蒸汽释放热量q32426.75#低加凝结水焓升τ4136.25段抽汽蒸汽释放