300MW机组改造热平衡图

F A B C
Y
0.98G
64.9T 2491.2H 14.60G
D
88.8T 2626.4H 30.48G
138.7T 2750.2H 27.35G
237.4T 2939.1H 43.72G
341.6T 3142.0H 44.58G
436.5T 3330.7H 36.22G
329.8T 3043.7H 87.19G
F A B C
Y
1.04G
65.0T 2496.3H 33.93G
D
89.7T 2634.6H 30.78G
143.2T 2759.0H 26.98G
242.3T 2948.6H 43.28G
345.5T 3149.7H 43.73G
438.2T 3333.7H 34.86G
333.2T 3050.6H 85.35G
315MW 亚临界机组热平衡图 工况 THA
1 : 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.
哈尔滨汽轮机厂有限责任公司
Li knsg2_1
43.16G 3142.0H 0.887P
Y X D
GV TV 0.00G 0.00G 16.70P 3396.9H 3.589P 3535.4H
177.5T 1.697P 763.5H HTR-3 # 204.2T
204.2T 879.1H
3.734P 246.3T HTR-2 1069.4H # 246.3T
6.026P HTR-1 275.8T
277.5T 1219.0H 966.92G
415.0H 39.1T 163.5H 125.60G 65.5T 274.2H 94.78G 89.8T 376.3H 65.92G 110.5T 463.5H 40.59G
k
538.0T 1015.22G 538.0T 841.99G BOILER # LOSS
BFPT 7258.4kW
0.941P 3150.1H 729.51G
ICV RSV HIP
0.0063P 2441.0H 36.85G 0.17G
DFLP 0.397P 0.17G 0.146P
D C
0.961P 0.10G
183.7T 779.5H 205.52G
211.2T 903.2H 165.11G
253.9T 1104.9H 77.92G
BFP 图例 : P = 压力 T = 温度 H=焓 G = 流量 单位 : MPaA ﾟC kJ/kg t/h
功率 热耗 汽耗
315000.0kW 8283.4kJ/kW.h 3.223kg/kW.h
F A B C
Y
1.03G
64.8T 2496.6H 33.43G
D
89.5T 2634.8H 30.46G
143.3T 2759.2H 26.71G
242.4T 2948.9H 42.82G
345.6T 3150.1H 43.24G
438.2T 3334.0H 34.42G
332.2T 3048.9H 84.34G
Li knsg2_1
34.84G 3151.6H 0.874P
Y X D
GV TV 0.41G 0.13G 16.70P 3396.9H 3.465P 3536.6H
k
538.0T 966.92G 538.0T 804.48G BOILER # LOSS
BFPT 6821.5kW
0.902P 3151.6H 698.48G
206.4T 888.8H
3.905P 248.9T HTR-2 1081.7H # 248.9T
6.325P HTR-1 279.0T
280.7T 1234.7H 1015.24G
415.0H 38.9T 162.9H 133.42G 66.4T 278.1H 99.98G 91.0T 381.0H 69.53G 111.8T 468.9H 42.82G
242.9T 2950.5H 40.59G
346.0T 3151.6H 40.79G
438.4T 3335.5H 32.33G
327.6T 3041.7H 79.30G
390.9T 3152.5H 70.27G
CO百度文库DENSER
0.0049P 0G MAKE UP 136.3H 32.5T 33.0T 138.0H 735.32G CP
85.6T 359.9H
0.140P HTR-6 # 109.2T
106.5T 0.381P 447.6H HTR-5 # 141.8T
139.1T 0.920P 586.0H DRTR # 176.3T 175.8T 747.1H 1025.00G
179.7T 1.789P 773.4H HTR-3 # 206.8T
7.25G 21.00G 3349.3H 13.357P 1.88P 6.58P
4.061P 0.10G
0.069P 0.0250P
13.75G
C D D B I A D
4.25G 2340.6H 601.15G
K
333.2T 3050.6H 849.54G
F
X
#
0.00G 0.90G G.R 0.86G 0.72G
ICV RSV HIP
0.0063P 2446.8H 34.84G 0.17G
DFLP 0.381P 0.17G 0.140P
D C
0.920P 0.10G
6.90G 20.04G 3338.6H 12.697P 1.79P 6.21P
3.850P 0.10G
0.066P 0.0238P
13.14G
185.3T 786.5H 201.17G
k
538.0T 1025.00G 538.0T 849.54G BOILER # LOSS
BFPT 7344.9kW
0.949P 3149.7H 735.75G
ICV RSV HIP
0.0063P 2439.9H 37.25G 0.17G
DFLP 0.401P 0.17G 0.147P
D C
0.969P 0.10G
397.9T 3163.6H 76.71G
CONDENSER
0.0049P 0G MAKE UP 136.3H 32.5T 33.0T 138.0H 774.96G CP
0.53G 5.14G
I
GC ##
33.4T 139.7H
0.024P HTR-8 63.8T
61.1T 0.066P 257.0H HTR-7 # 88.4T
184.9T 785.0H 198.57G
211.9T 906.6H 159.94G
254.5T 1107.7H 75.60G
BFP 图例 : P = 压力 T = 温度 H=焓 G = 流量 单位 : MPaA ﾟC kJ/kg t/h
功率 热耗 汽耗
327556.8kW 7951.2kJ/kW.h 3.099kg/kW.h
7.12G 20.96G 3347.9H 13.307P 1.84P 6.47P
3.987P 0.10G
0.067P 0.0249P
13.84G
C D D B I A D
4.18G 2408.8H 599.21G
K
329.8T 3043.7H 836.93G
F
X
#
0.00G 0.87G G.R 0.83G 0.72G
0.66G 4.89G
I
GC ##
33.5T 140.3H
0.023P HTR-8 62.8T
60.0T 0.063P 252.4H HTR-7 # 87.1T
84.3T 354.2H
0.133P HTR-6 # 107.7T
105.0T 0.362P 441.2H HTR-5 # 140.1T
137.3T 0.874P 578.4H DRTR # 174.1T 173.6T 737.6H 966.92G
85.4T 359.0H
0.139P HTR-6 # 109.0T
106.2T 0.378P 446.5H HTR-5 # 141.6T
138.8T 0.913P 584.7H DRTR # 176.0T 175.5T 745.5H 1015.24G
179.4T 1.773P 771.8H HTR-3 # 206.4T
206.8T 890.7H
3.940P 249.4T HTR-2 1084.2H # 249.4T
6.386P HTR-1 279.7T
281.3T 1237.8H 1025.00G
415.0H 38.9T 162.9H 134.98G 66.6T 278.8H 101.05G 91.2T 381.9H 70.27G 112.0T 469.9H 43.28G
k
538.0T 1015.22G 538.0T 836.93G BOILER # LOSS
BFPT 7502.7kW
0.915P 3142.0H 714.97G
ICV RSV HIP
0.0132P 2516.1H 43.16G 0.17G
DFLP 0.384P 0.17G 0.142P
D C
0.934P 0.10G
205.6T 885.6H
3.868P 248.4T HTR-2 1079.1H # 248.4T
6.276P HTR-1 278.5T
280.2T 1232.1H 1045.66G
415.0H 55.5T 232.1H 116.15G 66.5T 278.4H 101.55G 90.3T 378.1H 71.07G 110.9T 465.3H 43.72G
7.19G 21.04G 3349.6H 13.371P 1.87P 6.52P
4.026P 0.10G
0.069P 0.0248P
13.85G
C D D B I A D
4.21G 2340.9H 596.47G
K
332.2T 3048.9H 841.99G
F
X
#
0.00G 0.89G G.R 0.86G 0.72G
396.6T 3161.4H 75.60G
CONDENSER
0.0049P 0G MAKE UP 136.3H 32.5T 33.0T 138.0H 768.30G CP
0.53G 5.10G
I
GC ##
33.4T 139.7H
0.024P HTR-8 63.7T
60.9T 0.065P 256.2H HTR-7 # 88.2T
C D D B I A D
4.02G 2342.7H 573.27G
K
327.6T 3041.7H 804.48G
F
X
#
0.00G 0.86G G.R 0.81G 0.72G
F A B C
Y
0.95G
63.9T 2497.8H 30.83G
D
88.4T 2635.7H 28.85G
143.6T 2760.2H 25.34G
315MW 亚临界机组热平衡图 工况 TMCR
1 : 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.
哈尔滨汽轮机厂有限责任公司
Li knsg2_1
37.25G 3149.7H 0.920P
Y X D
GV TV 0.00G 0.00G 16.70P 3396.9H 3.655P 3534.7H
183.1T 776.7H 185.91G
209.8T 896.7H 149.56G
251.8T 1094.8H 70.27G
BFP 图例 : P = 压力 T = 温度 H=焓 G = 流量 单位 : MPaA ﾟC kJ/kg t/h
功率 热耗 汽耗
315000.0kW 7949.3kJ/kW.h 3.070kg/kW.h
315MW 亚临界机组热平衡图 工况 TRL
1 : 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.
哈尔滨汽轮机厂有限责任公司
Li knsg2_1
36.85G 3150.1H 0.913P
Y X D
GV TV 0.00G 0.00G 16.70P 3396.9H 3.623P 3535.0H
84.7T 356.1H
0.135P HTR-6 # 108.2T
105.4T 0.365P 443.0H HTR-5 # 140.4T
137.6T 0.887P 579.8H DRTR # 174.8T 174.3T 740.3H 1045.66G
178.2T 1.747P 766.7H HTR-3 # 205.6T
394.6T 3157.3H 77.92G
CONDENSER
0.0118P 30G MAKE UP 205.5H 49.1T 49.5T 207.3H 790.49G CP
0.53G 5.09G
I
GC ##
49.9T 208.9H
0.024P HTR-8 63.8T
61.0T 0.064P 256.6H HTR-7 # 87.5T