1#炉碳锰配料 (3).xlsx

1、元素MnFePSiC其它合计 合金成分65.40%26.09%0.51%1.30%6.20%0.50%100.00% 回收率77.50%93.00%85.00%3.17% 综合样65.54%25.86%0.55%1.06%6.49%0.50%100.00% 综合样回收率76.33%96.40%92.50%5.54%15.78% 理论合金成分66.54%24.95%0.51%0.61%6.99% 工艺控制Mn/FeMn/PR3Mn/SiO3Mn/Al2O4A/SMn/MgO 理论值3.01140.651.50 实际值3.20144.401.592.097.370.287.47 品种MnFePSi

2、O2CaOMgOAl2O3 1#平台矿33.000%4.822%0.232%10.677%23.052%4.070%2.42% 平台块矿27.000%2.920%0.189%6.200%23.070%3.770%0.58% 5#平台矿32.410%4.970%0.218%17.200%22.660%2.990%0.45% 富锰渣20.360%3.890%0.062%26.110%13.940%2.710%13.50% 3#炉回炉渣 40.490%7.820%0.006%38.000%7.480%1.750% 碳锰球团25.140%4.821%0.116%16.251%6.151%3.073%4

3、.00% 缅块矿28.100%3.680%0.113%33.280%0.620%3.430%13.50% 南非低锰41.10%6.78%0.056%4.72%9.24%1.35%0.57% 4#块矿30.652%5.954%0.138%23.798%9.550%2.946% 混矿代入300.1543.371.97124.46185.7237.5232.91 混矿成分30.89%4.46%0.203%12.81%19.12%3.86%3.39% 混料代入301.4194.172.09143.95188.6540.3540.91 混料成分28.03%8.76%0.19%13.39%17.55%3.

4、75%3.81% 铁矿1.359%51.219%0.100%4.898%1.933%2.679%1.13% 硅石96.00% 水洗碎铁 FePSiO2 贵州机焦(大通)79.17%18.89%1.95%9.23%12.80%0.08%47.08% 省内焦(科)79.16%17.40%3.44%13.00%6.67%0.14%54.04% 禄丰冶金焦83.63%14.54%1.83%4.50%7.81%0.14%48.71% 混焦代入131.7530.923.7618.583.590.0314.98 混焦成份79.17%18.58%2.26%10.05%11.60%0.09%48.44% 理论配

5、碳 元素MnFePSiO2CaOMgOAl2O3 入渣率14.50%5.00%10.00%88.00%95.00%95.00%95.00% 入渣量43.704.710.21126.68179.2138.3338.86 渣成分9.21%0.99%0.04%26.70%37.77%8.08%8.19% 元素MnFePSiC其它合计 合金成分65.40%26.09%0.51%1.30%6.20%0.50%100.00% 回收率77.50%93.00%85.00%2.84% 综合样65.54%25.86%0.55%1.06%6.49%0.50%100.00% 综合样回收率72.52%112.11%90

6、.93%4.96%15.78% 理论合金成分70.04%21.45%0.51%0.61%6.99% 工艺控制Mn/FeMn/PR3Mn/SiO3Mn/Al2O4A/SMn/MgO 理论值3.01140.651.50 实际值3.92149.411.441.986.680.307.61 品种MnFePSiO2CaOMgOAl2O3 1#碳锰配料计算 产 品 控 制 AVW 灰份成份 锰 矿 料 比 熔 剂 焦 炭 品种C 炉 渣 1#碳锰配料计算 产 品 控 制 144.40144.40 1#平台矿33.000%4.822%0.232%10.677%23.052%4.070%2.42% 平台块矿2

7、7.000%2.920%0.189%6.200%23.070%3.770%0.58% 5#平台矿32.410%4.970%0.218%17.200%22.660%2.990%0.45% 富锰渣20.360%3.890%0.062%26.110%13.940%2.710%13.50% 3#炉回炉渣 40.490%7.820%0.006%38.000%7.480%1.750% 碳锰球团25.140%4.821%0.116%16.251%6.151%3.073%4.00% 缅块矿28.100%3.680%0.113%33.280%0.620%3.430%13.50% 南非低锰41.10%6.78%0

8、.056%4.72%9.24%1.35%0.57% 4#块矿30.652%5.954%0.138%23.798%9.550%2.946% 混矿代入294.7742.351.89131.84174.7136.9236.64 混矿成分30.51%4.38%0.196%13.65%18.08%3.82%3.79% 混料代入295.5575.441.98149.64176.9738.8244.24 混料成分28.55%7.29%0.19%14.45%17.09%3.75%4.27% 铁矿1.359%51.219%0.100%4.898%1.933%2.679%1.13% 硅石96.00% 水洗碎铁 F

9、ePSiO2 贵州机焦(大通)79.17%18.89%1.95%9.23%12.80%0.08%47.08% 省内焦(科)79.16%17.40%3.44%13.00%6.67%0.14%54.04% 禄丰冶金焦83.63%14.54%1.83%4.50%7.81%0.14%48.71% 混焦代入131.7530.923.7618.583.590.0314.98 混焦成份79.17%18.58%2.26%10.05%11.60%0.09%48.44% 理论配碳 元素MnFePSiO2CaOMgOAl2O3 入渣率14.50%5.00%10.00%88.00%95.00%95.00%95.00%

10、 入渣量42.863.770.20131.69168.1236.8842.03 渣成分9.17%0.81%0.04%28.17%35.97%7.89%8.99% 元素MnFePSiC其它合计 合金成分65.40%26.09%0.51%1.30%6.20%0.50%100.00% 回收率77.50%93.00%85.00%2.98% 综合样65.54%25.86%0.55%1.06%6.49%0.50%100.00% 综合样回收率76.32%96.45%94.48%5.21%15.82% 理论合金成分66.55%24.94%0.49%0.61%6.97% 工艺控制Mn/FeMn/PR3Mn/Si

11、O3Mn/Al2O4A/SMn/MgO 理论值3.01140.651.50 实际值3.20147.521.441.976.770.297.48 品种MnFePSiO2CaOMgOAl2O3 1#平台矿33.000%4.822%0.232%10.677%23.052%4.070%2.42% 平台块矿27.000%2.920%0.189%6.200%23.070%3.770%0.58% 5#平台矿32.410%4.970%0.218%17.200%22.660%2.990%0.45% 富锰渣20.360%3.890%0.062%26.110%13.940%2.710%13.50% 3#炉回炉渣 4

12、0.490%7.820%0.006%38.000%7.480%1.750% 碳锰球团25.140%4.821%0.116%16.251%6.151%3.073%4.00% 缅块矿28.100%3.680%0.113%33.280%0.620%3.430%13.50% 南非低锰41.10%6.78%0.056%4.72%9.24%1.35%0.57% 4#块矿30.652%5.954%0.138%23.798%9.550%2.946% 混矿代入294.7742.351.89131.84174.7136.9236.64 混矿成分30.51%4.38%0.196%13.65%18.08%3.82%3

13、.79% 锰 矿 料 比 1#碳锰配料计算 产 品 控 制 炉 渣 锰 矿 料 比 熔 剂 焦 炭 品种CAVW 灰份成份 134.50134.50 混料代入296.0092.422.01150.39177.6439.5543.73 混料成分27.65%8.63%0.19%14.05%16.60%3.70%4.09% 铁矿1.359%51.219%0.100%4.898%1.933%2.679%1.13% 硅石96.00% 水洗碎铁 FePSiO2 贵州机焦(大通)79.17%18.89%1.95%9.23%12.80%0.08%47.08% 省内焦(科)79.16%17.40%3.44%13

14、.00%6.67%0.14%54.04% 禄丰冶金焦83.63%14.54%1.83%4.50%7.81%0.14%48.71% 混焦代入125.7630.013.1016.153.840.0214.13 混焦成份79.17%18.89%1.95%9.23%12.80%0.08%47.08% 理论配碳 元素MnFePSiO2CaOMgOAl2O3 入渣率14.50%5.00%10.00%88.00%95.00%95.00%95.00% 入渣量42.924.620.20132.35168.7637.5841.54 渣成分9.13%0.98%0.04%28.14%35.89%7.99%8.83%

15、141.40141.40 炉 渣 AVW 灰份成份 锰 矿 料 比 熔 剂 焦 炭 品种C 批料产量 351.04 一、锰矿 其他项 1#平台矿 平台块矿 5#平台矿 CH2O配比R3Mn/FeMn/P比例富锰渣 0.511%6502.5406.8441.42265.0%3#炉回炉渣 8.375%1404.3299.2471.42914.0%碳锰球团 0.542%1.4916.5211.4870.0%缅块矿 2.400%0.6385.2343.2840.0%南非低锰 0.100%0.2435.17867.4830.0%4#块矿 3.30%4.111%1100.5685.2152.16711.0

16、%二、焦碳 8.900%1000.1227.6362.48710.0%贵州机焦(大通) 1.20%2.2446.0627.3390.0%省内焦(科) 0.433%0.5255.1482.2210.0%禄丰冶金焦 3.4828.4710001.7946.9211.525三、动力 0.36%2.85%1.7946.9211.525水 3.4850.8711261.5913.2011.444电 0.32%4.52%1.5913.2011.444四、辅料 3.978%960.9420.0270.136铁矿 0.50%0硅石 30水洗碎铁 电极糊 CaOMgOAl2O3五、工资 3.95%0.71%20

17、.25%14578.4% 六、制造费用 2.71%3.00%31.73%4021.6%合 计 4.34%4.68%29.76%00.0% 1.150.366.96185 3.71%1.16%22.50% 446.04474.52 R3=1.72 批料产量 327.05 一、锰矿 其他项 1#平台矿 平台块矿 5#平台矿 CH2O配比R3Mn/FeMn/P比例富锰渣 成本项目 灰份成份 配比比例 合计渣量 （校称料比10批） 成本项目 202.76 0.511%5802.5406.8441.42258.0%3#炉回炉渣 8.375%1604.3299.2471.42916.0%碳锰球团 0.54

18、2%1.4916.5211.4870.0%缅块矿 2.400%0.6385.2343.2840.0%南非低锰 0.100%0.2435.17867.4830.0%4#块矿 3.30%4.111%1200.5685.2152.16712.0%二、焦碳 8.900%1400.1227.6362.48714.0%贵州机焦(大通) 1.20%2.2446.0627.3390.0%省内焦(科) 0.433%0.5255.1482.2210.0%禄丰冶金焦 3.8033.7610001.6056.9611.557三、动力 0.39%3.38%1.6056.9611.557水 3.8054.7310901.

19、4423.9181.494电 0.37%5.02%1.4423.9181.494四、辅料 3.978%600.9420.0270.136铁矿 0.50%0硅石 30水洗碎铁 电极糊 CaOMgOAl2O3五、工资 3.95%0.71%20.25%14578.4% 六、制造费用 2.71%3.00%31.73%4021.6%合 计 4.34%4.68%29.76%00.0% 1.150.366.96185 3.71%1.16%22.50% 439.35467.40 R3=1.56 批料产量 344.68 一、锰矿 其他项 1#平台矿 平台块矿 5#平台矿 CH2O配比R3Mn/FeMn/P比例富

20、锰渣 0.511%5802.5406.8441.42258.0%3#炉回炉渣 8.375%1604.3299.2471.42916.0%碳锰球团 0.542%1.4916.5211.4870.0%缅块矿 2.400%0.6385.2343.2840.0%南非低锰 0.100%0.2435.17867.4830.0%4#块矿 3.30%4.111%1200.5685.2152.16712.0%二、焦碳 8.900%1400.1227.6362.48714.0%贵州机焦(大通) 1.20%2.2446.0627.3390.0%省内焦(科) 0.433%0.5255.1482.2210.0%禄丰冶金

21、焦 3.8033.7610001.6056.9611.557三、动力 0.39%3.38%1.6056.9611.557水 成本项目 合计渣量 灰份成份 配比比例 188.87 3.8053.6511241.4443.2031.475电 0.35%4.77%1.4443.2031.475四、辅料 3.978%940.9420.0270.136铁矿 0.50%0硅石 30水洗碎铁 电极糊 CaOMgOAl2O3五、工资 3.95%0.71%20.25%175100.0% 六、制造费用 2.71%3.00%31.73%0.0%合 计 4.34%4.68%29.76%00.0% 1.190.216.

22、08175 3.95%0.71%20.25% 442.04470.25 R3=1.56 比例 196.77 合计渣量 灰份成份 配比 37000 #2.7682.6600.8550.8192,644.282,531.14# # 199.34199.34 3,130.001.8421.7290.6080.5711,902.791,785.8868160.85# 2,000.000.3650.3720.0990.101197.32201.1013520.37# 2,810.000.0000.0000.0000.0000.000.000.000.00 3,880.000.0000.0000.0000

23、.0000.000.000.000.00 21.490.0000.0000.0000.0000.000.000.000.00 3,517.000.3000.2930.0760.074265.67258.7111117.52# 3,819.000.2600.2660.0730.075278.50285.459602.07# 4,780.000.0000.0000.0000.0000.000.000.000.00 1,200.000.0000.0000.0000.0000.000.000.000.00 1,951.180.4740.497924.99969.42# 1,970.000.3750.3

24、90738.62767.3913872.57# 1,880.000.0990.107186.37202.023667.97# 1,910.000.0000.0000.000.000.000.00 1,473.951,346.54# 2.503.5003.4008.758.50# # 0.443330.0003041.0001,465.201,338.04# # 0.359280.39292.60# 660.000.2730.280180.49184.8010118.54# 190.000.0000.000.000.000.00 0.0850.000.003162.040.00 3,850.00

25、0.0280.02899.90107.801036.00# 141.79141.79# 六、制造费用209.11209.11# 5,964.0090.140274.0575,873.865,689.94# 37000 #2.9542.6600.9010.8092,794.082,505.25# # 199.34199.34 3,130.001.7641.5430.5820.5091,822.441,593.5665282.36# 2,000.000.4480.4260.1210.115242.06229.8216585.43# 2,810.000.0000.0000.0000.0000.000

26、.000.000.00 3,880.000.0000.0000.0000.0000.000.000.000.00 原料计划及产生成本分析 原料单价 （元/t) 理论原料 单耗 （t/t)干 实际原料 单耗 （t/t)干 理论金属 单耗 （t/t) 实际金属 单耗 （t/t) 理论单位 成本（元 /t) 实际单位 成本（元 /t) 本月计划 消耗（t) 计划总成 本 （元） 理论单位 成本（元 /t) 实际单位 成本（元 /t) 本月计划 消耗（t) 原料计划及产生成本分析 原料单价 （元/t) 理论原料 单耗 （t/t)干 计划总成 本 （元） 实际原料 单耗 （t/t)干 理论金属 单耗 （

27、t/t) 实际金属 单耗 （t/t) 21.490.0000.0000.0000.0000.000.000.000.00 3,517.000.3520.3190.0880.080311.08282.2313017.96# 3,819.000.3900.3720.1100.105418.50399.6414429.10# 4,780.000.0000.0000.0000.0000.000.000.000.00 1,200.000.0000.0000.0000.0000.000.000.000.00 1,951.180.5090.497992.85969.42# 1,970.000.4020.39

28、0792.81767.3914890.29# 1,880.000.1060.107200.05202.023937.06# 1,910.000.0000.0000.000.000.000.00 1,473.951,346.54# 2.503.5003.4008.758.50# # 0.443330.0003041.0001,465.201,338.04# # 0.275220.98292.60# 660.000.1830.280121.08184.806788.03# 190.000.0000.000.000.000.00 0.0920.000.003394.020.00 3,850.000.

29、0280.02899.90107.801036.00# 141.79141.79# 六、制造费用209.11209.11# 5,964.00-68.103299.9546,032.105,664.05# 37000 #2.8032.6600.8550.8092,651.142,505.25# # 199.34199.34 3,130.001.6741.5430.5520.5091,729.211,593.5661942.80# 2,000.000.4250.4260.1150.115229.68229.8215736.99# 2,810.000.0000.0000.0000.0000.000.

30、000.000.00 3,880.000.0000.0000.0000.0000.000.000.000.00 21.490.0000.0000.0000.0000.000.000.000.00 3,517.000.3340.3190.0840.080295.17282.2312352.01# 3,819.000.3700.3720.1040.105397.09399.6413690.97# 4,780.000.0000.0000.0000.0000.000.000.000.00 1,200.000.0000.0000.0000.0000.000.000.000.00 1,970.000.46

31、10.497907.89979.09# 1,970.000.4610.497907.89979.0917051.72# 1,880.000.0000.0000.000.000.000.00 1,910.000.0000.0000.000.000.000.00 1,473.951,346.54# 2.503.5003.4008.758.50# # 实际金属 单耗 （t/t) 理论单位 成本（元 /t) 实际单位 成本（元 /t) 本月计划 消耗（t) 计划总成 本 （元） 原料计划及产生成本分析 原料单价 （元/t) 理论原料 单耗 （t/t)干 实际原料 单耗 （t/t)干 理论金属 单耗 （

32、t/t) 0.443330.0003041.0001,465.201,338.04# # 0.360279.89292.60# 660.000.2730.280179.99184.8010090.57# 190.000.0000.000.000.000.00 0.0870.000.003220.390.00 3,850.000.0280.02899.90107.801036.00# 141.79141.79# 六、制造费用209.11209.11# 5,964.00100.883290.2835,863.125,673.72# 元素MnFePSiC其它合计 合金成分65.40%26.09%0.

33、51%1.30%6.20%0.50%100.00% 回收率77.50%93.00%85.00%2.84% 综合样65.54%25.86%0.55%1.06%6.49%0.50%100.00% 综合样回收率72.52%112.11%90.93%4.96%15.78% 理论合金成分70.04%21.45%0.51%0.61%6.99% 工艺控制Mn/FeMn/PR3Mn/SiO3Mn/Al2O4A/SMn/MgO 理论值3.01140.651.50 实际值3.92149.411.441.986.680.307.61 品种MnFePSiO2CaOMgOAl2O3 1#平台矿33.000%4.822%

34、0.232%10.677%23.052%4.070%2.42% 平台块矿27.000%2.920%0.189%6.200%23.070%3.770%0.58% 5#平台矿32.410%4.970%0.218%17.200%22.660%2.990%0.45% 富锰渣20.360%3.890%0.062%26.110%13.940%2.710%13.50% 3#炉回炉渣 40.490%7.820%0.006%38.000%7.480%1.750% 碳锰球团25.140%4.821%0.116%16.251%6.151%3.073%4.00% 缅块矿28.100%3.680%0.113%33.28

35、0%0.620%3.430%13.50% 南非低锰41.10%6.78%0.056%4.72%9.24%1.35%0.57% 4#块矿30.652%5.954%0.138%23.798%9.550%2.946% 混矿代入294.7742.351.89131.84174.7136.9236.64 混矿成分30.51%4.38%0.196%13.65%18.08%3.82%3.79% 混料代入295.5575.441.98149.64176.9738.8244.24 混料成分28.55%7.29%0.19%14.45%17.09%3.75%4.27% 铁矿1.359%51.219%0.100%4.

36、898%1.933%2.679%1.13% 硅石96.00% 水洗碎铁 FePSiO2 贵州机焦(大通)79.17%18.89%1.95%9.23%12.80%0.08%47.08% 省内焦(科)79.16%17.40%3.44%13.00%6.67%0.14%54.04% 禄丰冶金焦83.63%14.54%1.83%4.50%7.81%0.14%48.71% 混焦代入131.7530.923.7618.583.590.0314.98 混焦成份79.17%18.58%2.26%10.05%11.60%0.09%48.44% 理论配碳 元素MnFePSiO2CaOMgOAl2O3 入渣率14.5

37、0%5.00%10.00%88.00%95.00%95.00%95.00% 入渣量42.863.770.20131.69168.1236.8842.03 渣成分9.17%0.81%0.04%28.17%35.97%7.89%8.99% 炉 渣 VW 灰份成份 134.50134.50 锰 矿 料 比 熔 剂 焦 炭 品种CA 1#碳锰配料计算 产 品 控 制 批料产量 327.05 一、锰矿 其他项 1#平台矿 平台块矿 5#平台矿 CH2O配比R3Mn/FeMn/P比例富锰渣 0.511%5802.5406.8441.42258.0%3#炉回炉渣 8.375%1604.3299.2471.4

38、2916.0%碳锰球团 0.542%1.4916.5211.4870.0%缅块矿 2.400%0.6385.2343.2840.0%南非低锰 0.100%0.2435.17867.4830.0%4#块矿 3.30%4.111%1200.5685.2152.16712.0%二、焦碳 8.900%1400.1227.6362.48714.0%贵州机焦(大通) 1.20%2.2446.0627.3390.0%省内焦(科) 0.433%0.5255.1482.2210.0%禄丰冶金焦 3.8033.7610001.6056.9611.557三、动力 0.39%3.38%1.6056.9611.557水

39、 3.8054.7310901.4423.9181.494电 0.37%5.02%1.4423.9181.494四、辅料 3.978%600.9420.0270.136铁矿 0.50%0硅石 30水洗碎铁 电极糊 CaOMgOAl2O3五、工资 3.95%0.71%20.25%14578.4% 六、制造费用 2.71%3.00%31.73%4021.6%合 计 4.34%4.68%29.76%00.0% 1.150.366.96185 3.71%1.16%22.50% 439.35467.40 R3=1.56 合计渣量 灰份成份 配比比例 188.87 校称 成本项目 37000 #2.954

40、2.6600.9010.8092,794.082,505.25# # 199.34199.34 3,130.001.7641.5430.5820.5091,822.441,593.5665282.36# 2,000.000.4480.4260.1210.115242.06229.8216585.43# 2,810.000.0000.0000.0000.0000.000.000.000.00 3,880.000.0000.0000.0000.0000.000.000.000.00 21.490.0000.0000.0000.0000.000.000.000.00 3,517.000.3520.3

41、190.0880.080311.08282.2313017.96# 3,819.000.3900.3720.1100.105418.50399.6414429.10# 4,780.000.0000.0000.0000.0000.000.000.000.00 1,200.000.0000.0000.0000.0000.000.000.000.00 1,951.180.5090.497992.85969.42# 1,970.000.4020.390792.81767.3914890.29# 1,880.000.1060.107200.05202.023937.06# 1,910.000.0000.

42、0000.000.000.000.00 1,473.951,346.54# 2.503.5003.4008.758.50# # 0.443330.0003041.0001,465.201,338.04# # 0.275220.98292.60# 660.000.1830.280121.08184.806788.03# 190.000.0000.000.000.000.00 0.0920.000.003394.020.00 3,850.000.0280.02899.90107.801036.00# 141.79141.79# 六、制造费用209.11209.11# 5,964.00-68.103

43、299.9546,032.105,664.05# 实际金属 单耗 （t/t) 理论单位 成本（元 /t) 实际单位 成本（元 /t) 本月计划 消耗（t) 计划总成 本 （元） 原料计划及产生成本分析 原料单价 （元/t) 理论原料 单耗 （t/t)干 实际原料 单耗 （t/t)干 理论金属 单耗 （t/t) 元素MnFePSiC其它合计 合金成分65.40%26.09%0.51%1.30%6.20%0.50%100.00% 回收率77.50%93.00%85.00%3.22% 综合样65.54%25.86%0.55%1.06%6.49%0.50%100.00% 综合样回收率77.07%93.

44、99%94.15%5.63%15.86% 理论合金成分65.90%25.59%0.50%0.61%6.96% 工艺控制Mn/FeMn/PR3Mn/SiO3Mn/Al2O4A/SMn/MgO 理论值3.01140.651.50 实际值3.09145.571.452.1113.880.158.06 品种MnFePSiO2CaOMgOAl2O3 1#平台矿33.000%4.822%0.232%10.677%23.052%4.070%2.42% 平台块矿27.000%2.920%0.189%6.200%23.070%3.770%0.58% 5#平台矿32.410%4.970%0.218%17.200%

45、22.660%2.990%0.45% 富锰渣20.360%3.890%0.062%26.110%13.940%2.710%13.50% 3#炉回炉渣 40.490%7.820%0.006%38.000%7.480%1.750% 碳锰球团25.140%4.821%0.116%16.251%6.151%3.073%4.00% 缅块矿28.100%3.680%0.113%33.280%0.620%3.430%13.50% 金隆水洗 矿 27.560%9.100%0.162%19.500%0.360%1.810% 4#块矿30.652%5.954%0.138%23.798%9.550%2.946% 混

46、矿代入273.5748.641.78111.73152.0531.8412.99 混矿成分28.52%5.07%0.186%11.65%15.85%3.32%1.35% 混料代入274.5988.851.89130.36154.6534.0619.78 混料成分26.14%8.46%0.18%12.41%14.72%3.24%1.88% 铁矿1.359%51.219%0.100%4.898%1.933%2.679%1.13% 硅石96.00% 水洗碎铁 FePSiO2 贵州机焦(大通)79.20%18.52%2.28%7.80%6.28%0.10%50.95% 省内焦(科)79.16%17.4

47、0%3.44%13.00%6.67%0.14%54.04% 禄丰冶金焦83.63%14.54%1.83%4.50%7.81%0.14%48.71% 混焦代入125.6029.373.6213.421.840.0314.96 混焦成份79.20%18.52%2.28%7.80%6.28%0.10%50.95% 理论配碳 元素MnFePSiO2CaOMgOAl2O3 入渣率14.50%5.00%10.00%88.00%95.00%95.00%95.00% 入渣量39.824.440.19114.72146.9232.3618.79 渣成分10.11%1.13%0.05%29.12%37.29%8.21%4.77% 炉 渣 VW 灰份成份 132.14132.14 锰 矿 料 比 熔 剂 焦 炭 品种CA 1#碳锰配料计算 产 品 控 制 批料产量 322.92 一、锰矿 其他项 1#平台矿 平台块矿 5#平台矿 CH2O配比R3Mn/FeMn/P比例富锰渣 0.511%2602.5406.8441.42226.0%3#炉回炉渣 8.375%4004.3299.2471.42940.0%碳锰球团 0.542%1.4916.5211.48