300MW机组改造热平衡图

Liknsg2_134.84G3151.6HGVTV0.874P0.41G16.70P538.0T0.13G3396.9H966.92G0.902P3.465P538.0TBFPT3151.6H3536.6H804.48G6821.5kW698.48GICVRSVBOILER#HIP0.0063P6.90G20.04G2446.8HDFLP3338.6H12.697P34.84G0.381P0.920P1.79P6.21P3.850P0.17G0.17G0.140P0.10G0.10G0.066P13.14G0.0238P4.02G327.6T2342.7H3041.7H573.27G804.48G#0.00G0.86GG.R0.81G0.72G0.95G63.9T88.4T143.6T242.9T346.0T438.4T327.6T390.9T2497.8H2635.7H2760.2H2950.5H3151.6H3335.5H3041.7H3152.5H30.83G28.85G25.34G40.59G40.79G32.33G79.30G70.27GCONDENSER0.0049P0.66G4.89G0GMAKEUP136.3H32.5T33.0T33.5T0.023P60.0T0.063P84.3T0.133P105.0T0.362P137.3T0.874P177.5T1.697P204.2T3.734P246.3T6.026P277.5T138.0HGC140.3HHTR-8252.4HHTR-7354.2HHTR-6441.2HHTR-5578.4HDRTR763.5HHTR-3879.1HHTR-21069.4HHTR-11219.0H735.32G########966.92GCP62.8T87.1T107.7T140.1T174.1T204.2T246.3T275.8T415.0H173.6T39.1T65.5T89.8T110.5T737.6H183.1T209.8T251.8T163.5H274.2H376.3H463.5H966.92G776.7H896.7H1094.8H125.60G94.78G65.92G40.59G185.91G149.56G70.27GBFP图例:单位:P=压力MPaAT=温度ﾟCH=焓kJ/kg功率315000.0kW315MW亚临界机组热平衡图G=流量t/h热耗7949.3kJ/kW.h3.070kg/kW.h工况THA1:计算采用IFC67水蒸汽表2:无加热器散热损失3:计算基于阀点位置.汽耗哈尔滨汽轮机厂有限责任公司LOSSBIADFDDXkDFABCDCCDYIKYXLiknsg2_143.16G3142.0HGVTV0.887P0.00G16.70P538.0T0.00G3396.9H1015.22G0.915P3.589P538.0TBFPT3142.0H3535.4H836.93G7502.7kW714.97GICVRSVBOILER#HIP0.0132P7.12G20.96G2516.1HDFLP3347.9H13.307P43.16G0.384P0.934P1.84P6.47P3.987P0.17G0.17G0.142P0.10G0.10G0.067P13.84G0.0249P4.18G329.8T2408.8H3043.7H599.21G836.93G#0.00G0.87GG.R0.83G0.72G0.98G64.9T88.8T138.7T237.4T341.6T436.5T329.8T394.6T2491.2H2626.4H2750.2H2939.1H3142.0H3330.7H3043.7H3157.3H14.60G30.48G27.35G43.72G44.58G36.22G87.19G77.92GCONDENSER0.0118P0.53G5.09G30GMAKEUP205.5H49.1T49.5T49.9T0.024P61.0T0.064P84.7T0.135P105.4T0.365P137.6T0.887P178.2T1.747P205.6T3.868P248.4T6.276P280.2T207.3HGC208.9HHTR-8256.6HHTR-7356.1HHTR-6443.0HHTR-5579.8HDRTR766.7HHTR-3885.6HHTR-21079.1HHTR-11232.1H790.49G########1045.66GCP63.8T87.5T108.2T140.4T174.8T205.6T248.4T278.5T415.0H174.3T55.5T66.5T90.3T110.9T740.3H183.7T211.2T253.9T232.1H278.4H378.1H465.3H1045.66G779.5H903.2H1104.9H116.15G101.55G71.07G43.72G205.52G165.11G77.92GBFP图例:单位:P=压力MPaAT=温度ﾟCH=焓kJ/kg功率315000.0kW315MW亚临界机组热平衡图G=流量t/h热耗8283.4kJ/kW.h3.223kg/kW.h工况TRL1:计算采用IFC67水蒸汽表2:无加热器散热损失3:计算基于阀点位置.LOSS汽耗哈尔滨汽轮机厂有限责任公司BIADFDDXkDFABCDCCDYIKYXLiknsg2_136.85G3150.1HGVTV0.913P0.00G16.70P538.0T0.00G3396.9H1015.22G0.941P3.623P538.0TBFPT3150.1H3535.0H841.99G7258.4kW729.51GICVRSVBOILER#HIP0.0063P7.19G21.04G2441.0HDFLP3349.6H13.371P36.85G0.397P0.961P1.87P6.52P4.026P0.17G0.17G0.146P0.10G0.10G0.069P13.85G0.0248P4.21G332.2T2340.9H3048.9H596.47G841.99G#0.00G0.89GG.R0.86G0.72G1.03G64.8T89.5T143.3T242.4T345.6T438.2T332.2T396.6T2496.6H2634.8H2759.2H2948.9H3150.1H3334.0H3048.9H3161.4H33.43G30.46G26.71G42.82G43.24G34.42G84.34G75.60GCONDENSER0.0049P0.53G5.10G0GMAKEUP136.3H32.5T33.0T33.4T0.024P60.9T0.065P85.4T0.139P106.2T0.378P138.8T0.913P179.4T1.773P206.4T3.905P248.9T6.325P280.7T138.0HGC139.7HHTR-8256.2HHTR-7359.0HHTR-6446.5HHTR-5584.7HDRTR771.8HHTR-3888.8HHTR-21081.7HHTR-11234.7H768.30G########1015.24GCP63.7T88.2T109.0T141.6T176.0T206.4T248.9T279.0T415.0H175.5T38.9T66.4T91.0T111.8T745.5H184.9T211.9T254.5T162.9H278.1H381.0H468.9H1015.24G785.0H906.6H1107.7H133.42G99.98G69.53G42.82G198.57G159.94G75.60GBFP图例:单位:P=压力MPaAT=温度ﾟCH=焓kJ/kg功率327556.8kW315MW亚临界机组热平衡图G=流量t/h热耗7951.2kJ/kW.h3.099kg/kW.h工况TMCR1:计算采用IFC67水蒸汽表2:无加热器散热损失3:计算基于阀点位置.汽耗哈尔滨汽轮机厂有限责任公司LOSSBIADFDDXkDFABCDCCDYIKYXLiknsg2_137.25G3149.7HGVTV0.920P0.00G16.70P538.0T0.00G3396.9H1025.00G0.949P3.655P538.0TBFPT3149.7H3534.7H849.54G7344.9kW735.75GICVRSVBOILER#HIP0.0063P7.25G21.00G2439.9HDFLP3349.3H13.357P37.25G0.401P0.969P1.88P6.58P4.061P0.17G0.17G0.147P0.10G0.10G0.069P13.75G0.0250P4.25G333.2T2340.6H3050.6H601.15G849.54G#0.00G0.90GG.R0.86G0.72G1.04G65.0T89.7T143.2T242.3T345.5T438.2T333.2T397.9T2496.3H2634.6H2759.0H2948.6H3149.7H3333.7H3050.6H3163.6H33.93G30.78G26.98G43.28G43.73G34.86G85.35G76.71GCONDENSER0.0049P0.53G5.14G0GMAKEUP136.3H32.5T33.0T33.4T0.024P61.1T0.066P85.6T0.140P106.5T0.381P139.1T0.920P179.7T1.789P206.8T3.940P249.4T6.386P281.3T138.0HGC139.7HHTR-8257.0HHTR-7359.9HHTR-6447.6HHTR-5586.0HDRTR773.4HHTR-3890.7HHTR-21084.2HHTR-11237.8H774.96G########1025.00GCP63.8T88.4T109.2T141.8T176.3T206.8T249.4T279.7T415.0H175.8T38.9T66.6T91.2T112.0T747.1H185.3T212.4T255.0T162.9H278.8H381.9H469.9H1025.00G786.5H908.5H1110.2H134.98G101.05G70.27G43.28G201.17G162.06G76.71GBFP图例:单位:P=压力MPaAT=温度ﾟCH=焓kJ/kg功率330000.0kW315MW亚临界机组热平衡图G=流量t/h热耗7952.4kJ/kW.h3.106kg/kW.h工况VWO1:计算采用IFC67水蒸汽表2:无加热器散热损失3:计算基于阀点位置.LOSS汽耗哈尔滨汽轮机厂有限责任公司BIADFDDXkDFABCDCCDYIKYXLiknsg2_126.54G3163.2HGVTV0.899P0.82G16.70P538.0T0.25G3396.9H793.30G0.928P3.416P538.0TBFPT3163.2H3537.1H780.45G5253.8kW715.18GICVRSVBOILER#HIP0.0063P6.88G16.73G2450.5HDFLP3307.9H10.693P26.54G0.392P0.947P1.83P5.75P3.795P0.17G0.17G0.143P0.10G0.10G0.068P9.85G0.0244P3.90G330.5T2346.8H3050.8H587.45G780.45G#0.00G0.88GG.R0.84G0.72G1.00G64.4T89.0T147.5T247.9T351.7T2503.2H2641.9H2767.9H2960.3H3163.2H31.64G29.36G25.81G41.31G44.67G0.00G0.00G0.00GCONDENSER0.0049P0.79G4.75G0G