2#炉少溶剂法生产.xlsx

1、元素MnFePSiC其它合计 合金成分65.50%25.65%0.350%1.50%6.50%0.50%100.00% 回收率60.00%95.00%85.00%8.00%7.71% 综合样0.00%99.50%0.00%0.00%0.00%0.50% 综合样回收率 0.00%384.57%0.00%0.00%16.35% 66.57%24.58%0.33%1.56% 工艺控制Mn/FeMn/PR3Mn/SiO3Mg/Al2O4S/AR初 理论值4.04265.120.70 实际值4.29284.53 品种MnFePSiO2CaOMgOAl2O3 平台块矿27.88%2.71%0.188%3.

2、54%24.07%3.42%0.58% 3#缅矿 30.37%7.48%0.150%22.00%5.62%2.57%13.78% 缅块矿 32.00%5.31%0.120%20.00%3.22%2.43%8.20% 碳锰球团25.42%4.24%0.119%14.22%5.80%2.97%4.00% 南非低锰38.00%6.39%0.056%7.14%1.25%2.22%10.95% 南非低锰36.93%16.54%0.073%2.87%0.66%1.64%0.40% 澳矿高铁35.82%16.43%0.079%11.54%0.00%0.56%1.55% 澳矿高锰45.60%4.52%0.07

3、5%11.72%0.00%1.80%0.00% 1#平台矿33.80%4.82%0.232%10.68%23.05%4.07%2.42% 混矿代入356.1477.121.20119.4464.3921.0120.88 混矿成分37.01%8.01%0.124%12.41%6.69%2.18%2.17% 混料代入356.1483.051.25133.8366.3722.4128.46 混料成分37.01%8.63%0.13%13.91%6.90%2.33%2.96% 铁矿1.28%51.01%0.096%5.41%1.82%2.67%1.13% 白云石32.75%21.54% 硅石95.66%

4、 FePSiO2 禄丰冶金焦83.63%14.54%1.83%4.50%7.81%0.14%48.71% 冶金焦77.91%18.77%3.32%8.60%8.00%0.16%49.85% 贵机76.30%21.52%2.18%8.60%19.26%0.16%39.29% 混焦代入127.5134.794.0415.655.930.0614.39 混焦成份76.65%20.92%2.43%8.60%17.04%0.16%41.37% 理论配碳 元素MnOFeOPSiO2CaOMgOAl2O3 入渣率30.00%3.00%10.00%89.00%95.00%95.00%97.00% 入渣量137

5、.923.200.13119.1163.0521.2927.61 渣成分36.30%0.84%0.03%31.35%16.60%5.60%7.27% 渣成分51.27%1.19%0.05%44.28%23.44%7.91%10.26% 元素MnFePSiC其它合计 合金成分65.50%25.65%0.350%1.50%6.50%0.50%100.00% 回收率60.00%95.00%85.00%8.00%7.82% 综合样0.00%99.50%0.00%0.00%0.00%0.50% 综合样回收率 0.00%388.98%0.00%0.00%16.29% 66.85%24.30%0.34%1.

6、53% 工艺控制Mn/FeMn/PR3Mn/SiO3Mg/Al2O4S/AR初 理论值4.04265.120.70 实际值4.36281.83 产 品 控 制 国标（少溶剂）配料计算 炉 渣 VW 灰份成份 127.59127.59 A 锰 矿 料 比 熔 剂 焦 炭 品种C 国标（少溶剂）配料计算 产 品 控 制 品种MnFePSiO2CaOMgOAl2O3 平台块矿27.88%2.71%0.188%3.54%24.07%3.42%0.58% 3#缅矿 30.37%7.48%0.150%22.00%5.62%2.57%13.78% 缅块矿 32.00%5.31%0.120%20.00%3.2

7、2%2.43%8.20% 碳锰球团25.42%4.24%0.119%14.22%5.80%2.97%4.00% 南非低锰38.00%6.39%0.056%7.14%1.25%2.22%10.95% 南非低锰36.93%16.54%0.073%2.87%0.66%1.64%0.40% 澳矿高铁35.82%16.43%0.079%11.54%0.00%0.56%1.55% 澳矿高锰45.60%4.52%0.075%11.72%0.00%1.80%0.00% 1#平台矿33.80%4.82%0.232%10.68%23.05%4.07%2.42% 混矿代入367.8559.051.21119.446

8、5.3724.6524.44 混矿成分37.82%6.07%0.125%12.28%6.72%2.54%2.51% 混料代入368.3484.571.31135.9168.0527.0832.45 混料成分36.43%8.36%0.13%13.44%6.73%2.68%3.21% 铁矿1.28%51.01%0.096%5.41%1.82%2.67%1.13% 白云石32.75%21.54% 硅石95.66% FePSiO2 禄丰冶金焦83.63%14.54%1.83%4.50%7.81%0.14%48.71% 冶金焦77.91%18.77%3.32%8.60%8.00%0.16%49.85%

9、贵机76.30%21.52%2.18%8.60%19.26%0.16%39.29% 混焦代入127.5134.794.0415.655.930.0614.39 混焦成份76.65%20.92%2.43%8.60%17.04%0.16%41.37% 理论配碳 元素MnOFeOPSiO2CaOMgOAl2O3 入渣率30.00%3.00%10.00%89.00%95.00%95.00%97.00% 入渣量142.653.260.13120.9664.6425.7331.48 渣成分35.95%0.82%0.03%30.49%16.29%6.48%7.93% 炉 渣 VW 灰份成份 131.9313

10、1.93 A 锰 矿 料 比 熔 剂 焦 炭 品种C 批料产量5000 320.99321.1870614991.231 一、锰矿 其他 平台块矿 2,000.00 3#缅矿 5,718.00 缅块矿 3,380.00 CH2O配比比例Mn/FeMn/PR3碳锰球团 1,441.16 8.42%0.00%10.29148.307.77南非低锰 4,260.00 0.64%0.00%4.06202.470.37南非低锰 4,050.00 3.00%10010.00%6.03266.670.28澳矿高铁 4,580.00 3.90%3.26%707.00%6.00213.610.62澳矿高锰 4,

11、480.00 0.70%0.00%5.95678.570.491#平台矿 3,280.00 1.70%00.00%2.23505.890.80二、焦碳 6.50%29029.00%2.18453.420.05禄丰冶金焦 1,800.00 4.20%29029.00%10.09608.000.15冶金焦1,800.00 0.51%25025.00%7.01145.702.54贵机1,700.00 2.6437.5910001.00三、动力 0.27%3.76%水2.50 2.6437.591000电0.46 0.27%3.76%四、辅料 3.99%铁矿580.00 0.40%0白云石54.00

12、0.70%0硅石190.00 电极糊3,600.00 CaOMgOAl2O3比例 五、工资 4.34%4.68%29.76%00.00%六、制造费用 8.69%2.77%28.02%4021.98%合 计0.00 4.95%4.33%20.25%14278.02% 1.981.407.58182 5.69%4.02%21.78% 372.31379.9128.12%0.66% R3=0.71渣铁比1.18 R3=0.71渣铁比#DIV/0! 批料产量5000 330.60 一、锰矿 其他 平台块矿 2,000.00 3#缅矿 5,718.00 缅块矿 3,380.00 原料计划及产生成本分析

13、用澳矿高锰 成本项目 原料单价 （元/t) 合计渣量渣中Mn渣中Fe 灰份成份 配比 182 原料计划及产生成本分析 用澳矿高锰 成本项目 原料单价 （元/t) CH2O配比比例Mn/FeMn/PR3碳锰球团 1,441.16 8.42%0.00%10.29148.307.77南非低锰 4,260.00 0.64%0.00%4.06202.470.37南非低锰 4,050.00 3.00%20020.00%6.03266.670.28澳矿高铁 4,580.00 3.90%3.26%606.00%6.00213.610.62澳矿高锰 4,480.00 0.70%0.00%5.95678.570.

14、491#平台矿 3,280.00 1.70%11011.00%2.23505.890.80二、焦碳 6.50%0.00%2.18453.420.05禄丰冶金焦 1,800.00 4.20%39039.00%10.09608.000.15冶金焦1,800.00 0.51%24024.00%7.01145.702.54贵机1,700.00 2.2627.4310001.00三、动力 0.23%2.74%水2.50 2.2629.031040电0.46 0.22%2.79%四、辅料 3.99%40铁矿580.00 0.40%0白云石54.00 0.70%0硅石190.00 电极糊3,600.00 C

15、aOMgOAl2O3比例 五、工资 4.34%4.68%29.76%00.00%六、制造费用 8.69%2.77%28.02%4021.98%合 计0.00 4.95%4.33%20.25%14278.02% 1.981.407.58182 5.69%4.02%21.78% 388.85396.7927.85%0.64% R3=0.75渣铁比1.20 合计渣量渣中Mn渣中Fe 灰份成份 配比 188 2.9981.1106,900.2314991.23 0.00 0.0000.0000.000.00 0.0000.0000.000.00 0.3020.097326.851510.95 0.21

16、10.05477.291054.83 0.0000.0000.000.00 0.0000.0000.000.00 0.8450.3033,868.854223.64 0.8660.3951,768.134327.53 0.7750.262859.113874.29 0.518892.38#REF! 0.0000.00#REF! 0.114205.02#REF! 0.404687.37#REF! 1,346.50 5.00012.50#REF! 2900.0001,334.00#REF! 0.00082.80 0.0000.00#REF! 0.0000.00#REF! 0.0000.00#REF

17、! 0.02382.80#REF! 141.79 174.17 0.000.009,537.87 #REF! 2.9421.1134,297.6714709.04 0.00 0.0000.0000.000.00 0.0000.0000.000.00 0.5870.188634.692934.04 原料计划及产生成本分析 理论原料单 耗（t/t)干 量 理论金属 单耗 （t/t) 理论单位 成本（元 /t) 本月计划 消耗（t) 原料计划及产生成本分析 理论原料单 耗（t/t)干 量 理论金属 单耗 （t/t) 理论单位 成本（元 /t) 本月计划 消耗（t) 0.1760.04564.3287

18、7.85 0.0000.0000.000.00 0.3270.121489.191635.35 0.0000.0000.000.00 1.1300.5152,308.705650.60 0.7220.244800.773611.19 0.503866.44#REF! 0.0000.00#REF! 0.111199.06#REF! 0.393667.39#REF! 1,346.50 5.00012.50#REF! 2900.0001,334.00#REF! 0.121152.98 0.12170.18#REF! 0.0000.00#REF! 0.0000.00#REF! 0.02382.80#REF! 141.79 174.17 0.000.006,979.55 #REF!