月原料计划.xlsx

1、1#炉 成本项目理论原料单耗（t/t)干量原料比例本月计划消耗（t)计划产量5100 成本项目理论原料单耗（t/t)干量 一、锰矿2.797100.00%14264.42 一、锰矿2.797 其他项 1#平台矿1.092 1#平台矿1.09238.00%5570.57平台块矿0.476 平台块矿0.47618.00%2430.125#平台矿0.546 5#平台矿0.54619.00%2784.42富锰渣0.197 富锰渣0.1977.00%1006.673#炉回炉渣0.000 3#炉回炉渣0.0000.00%0.00碳锰球团0.222 碳锰球团0.2228.00%1130.32缅块矿 0.26

2、3 缅块矿 0.26310.00%1342.33南非低锰0.000 南非低锰0.0000.00%0.004#块矿0.000 4#块矿0.0000.00%0.00二、焦碳0.503 二、焦碳0.503禄丰焦0.188 禄丰焦0.18837.29%956.87省内焦0.000 省内焦0.0000.00%0.00贵机0.315 贵机0.31562.71%1608.93三、动力 三、动力水3.500 水3.5003.40017850.00电3330.000 电3330.0003041.000#四、辅料0.352 四、辅料0.352铁矿0.280 铁矿0.2800.2801429.26硅石0.000 硅

3、石0.0000.00水洗碎铁0.072 水洗碎铁0.072368.37电极糊0.028 电极糊0.0280.028142.80 1#碳锰配料计算 元素MnFePSiC其它 合金成分65.40%26.09%0.51%1.30%6.20%0.50% 回收率78.00%91.50%85.00%2.89% 综合样65.54%25.86%0.55%1.06%6.49%0.50% 综合样回收率76.40%96.27%92.80%5.04%18.11% 理论合金成分66.91%24.58%0.50%0.61%6.09% 工艺控制Mn/FeMn/PR3Mn/SiO3Mn/Al2O4A/S 理论值2.94139

4、.741.50 实际值3.19144.741.431.918.340.23 品种MnFePSiO2CaOMgO 1#平台矿33.000%4.822%0.232%10.677%23.052%4.070% 平台块矿27.000%2.920%0.189%6.200%23.070%3.770% 5#平台矿32.410%4.970%0.218%17.200%22.660%2.990% 富锰渣20.360%3.890%0.062%26.110%13.940%2.710% 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%

5、16.251%6.151%3.073% 缅块矿28.100%3.680%0.113%33.280%0.620%3.430% 南非低锰41.10%6.78%0.056%4.72%9.24%1.35% 4#块矿30.652%5.954%0.138%23.798%9.550%2.946% 产 品 控 制 锰 矿 料 比 混矿代入303.6145.071.97139.57186.5035.60 混矿成分31.09%4.61%0.202%14.29%19.10%3.65% 混料代入304.8595.462.11160.01189.0740.24 混料成分28.46%8.91%0.20%14.94%17.

6、65%3.76% 铁矿1.359%51.219%0.100%4.898%1.933%2.679% 硅石96.00% 水洗碎铁 灰份成份 FeP 冶金焦77.91%18.77%3.32%8.60%8.00%0.16% 省内焦79.16%17.40%3.44%13.00%6.67%0.14% 贵机(浩丰)(浩丰)78.270%18.980%2.750%9.100%11.47%0.13% 混焦代入131.6231.924.6216.843.660.04 混焦成份78.27%18.98%2.75%9.10%11.47%0.13% 理论配碳178.95 元素MnFeP SiO2CaOMgO 入渣率17.

7、00%5.00%10.00%88.00%88.00%95.00% 入渣量51.824.770.21140.81166.3838.22 渣成分10.74%0.99%0.04%29.17%34.47%7.92% 炉 渣 品种CAV 127.32127.32 锰 矿 料 比 熔 剂 焦 炭 W 原料比例本月计划消耗（t) 100.00%14264.42 38.00%5570.57 18.00%2430.12 19.00%2784.42 7.00%1006.67 0.00%0.00 8.00%1130.32 10.00%1342.33 0.00%0.00 0.00%0.00 2565.81 37.29

8、%956.87 0.00%0.00 62.71%1608.93 3.40017850.00 3041.00016983000.00 0.2801429.26 0.00 368.37 0.028142.80 合计批料产量 100.00%355.36 3.1376307 100.00%1.4070093 Mn/MgO 7.58 Al2O3CH2O配比 R3Mn/FeMn/P比例 2.42%0.511%500 2.5406.8441.42250.0% 3#炉回炉渣 0.58%8.375%804.3299.2471.4298.0% 0.45%0.542%2101.4916.5211.48721.0%

9、13.50%2.400%0.6385.2343.2840.0% 0.100%0.2435.17867.4830.0% 4.00%3.30%4.111%1200.5685.2152.16712.0% 13.50%8.900%900.1227.6362.4879.0% 0.57%1.20%2.2446.0627.3390.0% 0.433%0.5255.1482.2210.0%贵机(浩丰) 29.073.8023.3410001.5916.7361.538 2.98%0.39%2.33%1.5916.7361.538 36.573.8043.9511151.4333.1941.447 3.41%0

10、.35%3.94%1.4333.1941.447 1.13%3.978%950.9420.0270.136 0.50%0 20 SiO2CaOMgOAl2O3 49.85%8.69%2.77%28.02%0.0% 六、制造费用 54.04%2.71%3.00%31.73%00.0% 50.05%2.55%6.86%20.25%185100.0% 15.970.812.196.46185 50.05%2.55%6.86%20.25% Al2O3 95.00% 34.74453.68482.64 7.20% R3=1.45 合计渣量 配比比例 510014016.58229 一、锰矿 #2.748

11、2.6600.8540.8252,626.42 2,536.5414016.58 其他项199.34199.34 1#平台矿 3,130.001.4001.3300.4620.4391,445.87 1,373.767139.08 平台块矿 2,000.000.2060.2130.0560.057111.38 114.911051.96 5#平台矿 2,810.000.5880.559 0.1900.181535.27508.732997.48 富锰渣3,880.000.0000.0000.0000.0000.000.000.00 3#炉回炉渣 21.490.0000.0000.0000.00

12、00.000.000.00 碳锰球团 3,517.000.3240.3190.0810.080286.30 282.231651.38 缅块矿3,819.000.2310.2390.0650.067247.60256.911176.68 南非低锰 4,780.000.0000.0000.0000.0000.00 0.000.00 4#块矿1,200.000.0000.0000.0000.0000.000.000.00 二、焦碳 1,910.000.4730.497903.85 949.27 冶金焦1,970.000.0000.0000.000.000.00 省内焦1,880.000.0000.

13、0000.000.000.00 贵机(浩丰) 1,910.000.4730.497903.85 949.272534.70 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) 成本项目 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) 三、动力1,473.951,346.54 水2.503.5003.4008.758.5017850.00 电0.443330.0003041.0001,465.201,338.0416983000.00 四、辅料0.324276

14、.34292.60 铁矿660.000.2670.280176.44184.801363.39 硅石190.000.0000.000.000.00 水洗碎铁0.0560.000.00287.03 电极糊3,850.000.0280.02899.90107.80142.80 五、工资141.79141.79 六、制造费用 209.11209.11 合 计5,964.00133.204288.8145,830.805,675.19 43,173,805.49 22,345,317.85 2,103,929.09 8,422,915.92 0.00 0.00 5,807,905.39 4,493,7

15、37.23 0.00 0.00 4,841,277.00 0.00 0.00 4,841,277.00 计划总成本 （元） 7,517,145.00 44,625.00 7,472,520.00 1,449,618.71 899,838.71 0.00 0.00 549,780.00 723,129.00 1,066,461.00 58,771,436.20 原料计划及产生成本分析 成本项目理论原料单耗（t/t)干量原料比例本月计划消耗（t)计划产量 成本项目 一、锰矿2.971100.00% 18719.37 其他一、锰矿 1#平台矿 平台块矿0.0000.00%0.00平台块矿 3#缅矿

16、0.0000.00%0.005#平台矿 缅块矿 0.56920.20%3587.10富锰渣 碳锰球团0.1786.00%1122.553#炉回炉渣 富锰渣外高0.0000.00%0.00碳锰球团 南非低锰0.0000.00%0.00缅块矿 澳矿高铁0.31510.60%1985.65南非低锰 澳矿高锰1.15138.60%7253.344#块矿 1#平台矿0.75724.60%4770.72二、焦碳 二、焦碳0.5210.0003282.55禄丰焦 禄丰冶金焦0.14828.36%930.78省内焦 省外焦0.0000.00%0.00贵机 贵机0.37371.64%2351.77三、动力 三、

17、动力水 水5.0005.000电 电3917.3624350.460四、辅料 四、辅料0.000铁矿 铁矿0.0000.000硅石 白云石0.000水洗碎铁 硅石0.0000.000电极糊 电极糊0.0250.000157.50 元素MnFePSiC其它 合金成分65.40%26.09%0.51%1.30%6.20%0.50% 回收率77.00%91.50%85.00%2.90% 综合样65.54%25.86%0.55%1.06%6.49%0.50% 综合样回收率75.67%95.43%91.57%5.07%18.11% 理论合金成分66.69%24.80%0.51%0.61%6.09% 工艺

18、控制Mn/FeMn/PR3Mn/SiO3Mn/Al2O4A/S 理论值2.98141.561.50 实际值3.20144.211.471.938.590.23 品种MnFePSiO2CaOMgO 1#平台矿33.000%4.822%0.232%10.677%23.052%4.070% 平台块矿27.000%2.920%0.189%6.200%23.070%3.770% 5#平台矿32.410%4.970%0.218%17.200%22.660%2.990% 富锰渣20.360%3.890%0.062%26.110%13.940%2.710% 3#炉回炉渣40.490%7.820%0.006%3

19、8.000%7.480%1.750% 碳锰球团25.140%4.821%0.116%16.251%6.151%3.073% 缅块矿28.100%3.680%0.113%33.280%0.620%3.430% 南非低锰41.10%6.78%0.056%4.72%9.24%1.35% 4#块矿30.652%5.954%0.138%23.798%9.550%2.946% 混矿代入304.3345.221.99137.60188.7335.70 混矿成分31.13%4.63%0.203%14.08%19.31%3.65% 产 品 控 制 锰 矿 料 比 2#碳锰配料计算 混料代入305.5795.60

20、2.12158.04191.3140.33 混料成分28.51%8.92%0.20%14.74%17.85%3.76% 铁矿1.359%51.219%0.100%4.898%1.933%2.679% 硅石96.00% 水洗碎铁 FeP 冶金焦77.91%18.77%3.32%8.60%8.00%0.16% 省内焦79.16%17.40%3.44%13.00%6.67%0.14% 贵机(浩丰)(浩丰)78.270%18.980%2.750%9.100%11.47%0.13% 混焦代入131.6231.924.6216.843.660.04 混焦成份78.27%18.98%2.75%9.10%11

21、.47%0.13% 理论配碳 元素MnFeP SiO2CaOMgO 入渣率18.00%5.00%10.00%88.00%88.00%95.00% 入渣量55.004.780.21139.08168.3538.31 渣成分11.31%0.98%0.04%28.59%34.61%7.88% 锰 矿 料 比 熔 剂 焦 炭 炉 渣 126.44126.44 品种CAVW 6300 理论原料单耗（t/t)干量原料比例本月计划消耗（t) 2.971100.00%18719.37 0.00038.00%0.00 0.00018.00%0.00 0.56919.00%3587.10 0.1787.00%11

22、22.55 0.0000.00%0.00 0.0008.00%0.00 0.31510.00%1985.65 1.1510.00%7253.34 0.7570.00%4770.72 0.5213282.55 0.14828.36%930.78 0.0000.00%0.00 0.37371.64%2351.77 5.0003.40031500.00 3917.3623041.00024679380.26 0.000 0.0000.2800.00 0.0000.00 0.0000.00 0.0250.028157.50 合计批料产量 100.00%352.78 100.00% Mn/MgO 7.5

23、8 Al2O3CH2O配比 R3Mn/FeMn/P比例 2.42%0.511%5102.5406.8441.42251.0% 0.58%8.375%804.3299.2471.4298.0% 0.45%0.542%2101.4916.5211.48721.0% 13.50%2.400%0.6385.2343.2840.0% 0.100%0.2435.17867.4830.0% 4.00%3.30%4.111%1200.5685.2152.16712.0% 13.50%8.900%800.1227.6362.4878.0% 0.57%1.20%2.2446.0627.3390.0% 0.433%

24、0.5255.1482.2210.0% 28.093.8022.5010001.6316.7301.532 2.87%0.39%2.25%1.6316.7301.532 35.583.8043.1111151.4663.1961.442 3.32%0.35%3.87%1.4663.1961.442 1.13%3.978%950.9420.0270.136 0.50%0 20 SiO2CaOMgOAl2O3 49.85%8.69%2.77%28.02%0.0% 54.04%2.71%3.00%31.73%00.0% 50.05%2.55%6.86%20.25%185100.0% 15.970.8

25、12.196.46185 50.05%2.55%6.86%20.25% Al2O3 95.00% 33.80457.18486.37 6.95% R3=1.49 合计渣量 配比比例 灰份成份 177.72 1400 一、锰矿 #2.7712.6600.8630.8262,647.032,535.47 其他项199.34199.34 1#平台矿 3,130.001.4381.3570.4750.4481,485.57 1,401.23 矿耗平台块矿 2,000.000.2080.2130.0560.057112.20114.91 35#平台矿 2,810.000.5920.5590.1920.1

26、81539.18508.73 富锰渣3,880.000.0000.0000.0000.0000.000.00 1.4456403 3#炉回炉渣21.490.0000.0000.000 0.0000.000.00 0.2267671 碳锰球团 3,517.000.3260.3190.0820.080288.39282.23 0.5952637缅块矿3,819.000.2070.2130.0580.060221.69228.36 南非低锰 4,780.000.0000.0000.0000.0000.00 0.00 4#块矿1,200.000.0000.0000.0000.0000.000.00 0

27、.3401507 二、焦碳 1,910.000.4770.497910.46949.27 0.2267671冶金焦1,970.000.0000.0000.000.00 省内焦1,880.000.0000.0000.000.00 贵机(浩丰)1,910.000.4770.497910.46 949.27 三、动力1,473.951,346.54 水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) 成本项目 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

28、属 单耗 （t/t) 电0.443330.0003041.0001,465.201,338.04 四、辅料0.326277.63292.60 0.2692859铁矿660.000.2690.280177.73184.80 硅石190.000.0000.000.00 0.0566918 水洗碎铁0.057 0.000.00 电极糊3,850.000.0280.02899.90107.80 五、工资141.79141.79 六、制造费用 209.11209.11 合 计5,964.00104.691289.8855,859.315,674.12 3879.14# 2013.55# 290.89#

29、828.85# 0.000.00 0.000.00 456.63# 289.22# 0.000.00 0.000.00 # 0.000.00 0.000.00 695.80# # 4900.00# 本月计划 消耗（t) 计划总成 本 （元） # # # 377.00# 0.000.00 79.370.00 39.20# # # # 月份 炉号 产品种类 产量（t) 原料名称比例（%） 矿耗（t/t) 消耗（t) 平台块矿0.000 1#平台矿24.570.724320 4#矿0.000 南非块矿（低铁）0.000 澳块矿(高铁)10.580.311860 澳块矿(低铁)38.571.13678

30、0 缅 块 矿(高硅)20.140.593540 富锰渣(外购高锰)0.0000 富锰渣(外购低锰)0.000 5#平台矿0.000 3#回炉渣0.000 平台粉矿2.730.08480 1#平台粉矿0.340.0160 斗南3#精矿1.710.05300 缅粉矿1.370.04240 尾烧0.000 小计2.9317580 元素MnFePSiC其它合计 合金成分65.50%24.65%0.350%2.50%6.50%0.50%100.00% 回收率61.10%95.00%85.00%0.00%10.53% 综合样0.00%99.50%0.00%0.00%0.00%0.50% 综合样回收率 0

31、.00%404.07%0.00%0.00%15.99% 66.76%23.39%0.33%0.00% 工艺控制Mn/FeMn/PR3Mn/SiO3Mg/Al2O4S/AR初 理论值4.13260.350.70 实际值4.44285.12 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% 28.10%3.68%0.120%33.38%0.62%3.43%13.50% 碳锰球团26.17%4.80%0.117%16.18%6.1

32、9%3.17%4.00% 富锰渣外高38.00%2.33%0.053%18.00%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38.00%18.00%0.07%13.00%0.64%1.95%0.60% 澳矿高锰45.02%9.89%0.075%10.57%0.00%2.41%4.65% 1#平台矿33.80%4.82%0.232%10.68%23.05%4.07%2.42% 混矿代入355.7476.471.21149.4561.7829.0550.98 混矿成分37.04%7.96%0.126%15.56%

33、6.43%3.03%5.31% 混料代入355.7480.181.25165.6062.6031.2757.52 混料成分37.04%8.35%0.13%17.24%6.52%3.26%5.99% 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% 产 品 控 制 锰 矿 料 比 熔 剂 国标配料计算 灰份成份 品种CAVW 2#炉 少熔剂法 6000 备注：以上各种矿石消耗数量为达到建锰公司内控标准合格矿石的消耗

34、数量。 省内焦79.16%17.40%3.44%13.00%6.67%0.14%54.04% 贵机78.270%18.980%2.750%9.100%11.47%0.13%50.05% 混焦代入133.0532.264.6717.023.700.0416.15 混焦成份78.27%18.98%2.75%9.10%11.47%0.13%50.05% 理论配碳 元素MnOFeOP SiO2CaOMgOAl2O3 入渣率31.90%3.00%10.00%89.00%95.00%95.00%97.00% 入渣量146.493.090.12147.3859.4729.7055.79 渣成分29.83%0

35、.63%0.03%30.01%12.11%6.05%11.36% 焦 炭 炉 渣 132.34132.34 批料产量2100 325.60316.810226193.8077 一、锰矿 其他 平台块矿 2,000.00 3#缅矿4,340.00 3,819.00 CH2O配比比例Mn/FeMn/PR3碳锰球团800.00 8.42%0.00%10.29148.307.77富锰渣外高 4,050.00 0.64%0.00%4.06202.470.37南非低锰 4,050.00 8.90%20220.20%7.64234.170.12澳矿高铁 1,200.00 3.90%4.02%606.00%5

36、.45223.680.58澳矿高锰 4,060.00 0.70%00.00%16.31716.980.191#平台矿 3,130.00 1.70%00.00%2.23505.890.80二、焦碳 3.90%10610.60%2.11542.860.20禄丰冶金焦 1,880.00 3.60%38638.60%4.55600.270.23省内焦1,970.00 0.51%24624.60%7.01145.702.54贵机1,910.00 2.2539.6810001.00三、动力 0.23%3.97%水2.50 2.2539.681000电0.44 0.23%3.97%四、辅料 3.99%铁矿5

37、80.00 0.40%0白云石54.00 0.70%0硅石190.00 电极糊3,850.00 CaOMgOAl2O3比例 五、工资 4.34%4.68%29.76%0.00%六、制造费用 配比 用澳矿高锰 灰份成份 成本项目 原料单价 （元/t) 2.71%3.00%31.73%00.00%合 计6,852.00 2.55%6.86%20.25%187100.00% 0.822.216.53187149.6162 2.55%6.86%20.25%37.40 442.06491.1723.10%0.49% R3=0.61渣铁比1.51 合计渣量渣中Mn渣中Fe 186 2.949100.00%

38、1.0930.7734,242.152,812.636193.81#REF! 234.50234.50 0.0000.00%0.0000.0000.000.000.00#REF! 0.0000.00%0.0000.0000.000.000.00#REF! 0.56520.20%0.1590.156606.52596.321186.89#REF! 0.1776.00%0.0460.046141.5048.00371.43#REF! 0.0000.00%0.0000.0000.000.000.00#REF! 0.0000.00%0.0000.0000.000.000.00#REF! 0.31310

39、.60%0.1190.082375.43127.20657.01#REF! 1.14338.60%0.5150.2982,088.901,211.412399.96#REF! 0.75224.60%0.2540.190795.30595.191578.52#REF! 0.5220.000997.151,096.341096.34#REF! 0.0000.00%0.000.000.00#REF! 0.0000.00%0.000.000.00#REF! 0.522100.00%997.151,096.341096.34#REF! 1,736.141,926.70#REF! 5.0005.00012

40、.5012.50#REF!#REF! 3917.3624350.4601,723.641,914.20#REF!#REF! 0.00096.25335.89#REF! 0.0000.2130.00123.540.00#REF! 0.0000.000.000.00#REF! 0.0000.5300.00100.700.00#REF! 0.0250.02996.25111.6552.50#REF! 141.79141.79#REF! 209.11209.10#REF! 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

41、料计划及产生成本分析 理论原料单 耗（t/t)干 量 原料比例 理论金属 单耗 （t/t) -570.59-570.59329.55329.557,422.596,522.45#REF! # 原料计划及产生成本分析 成本项目理论原料单耗（t/t)干量实际原料单耗（t/t)干量本月计划消耗（t) 一、锰矿2.582100.00%20656.07 其他 平台块矿0.71928.67%5755.42 1#平台矿0.0000.00%0.00 缅块矿 0.0823.33%656.98 碳锰球团0.26210.00%2098.57 富锰渣外0.71526.67%5717.34 南非低锰0.33213.00

42、%2655.02 4#矿0.0000.00%0.00 澳矿高锰0.25510.00%2040.16 澳矿高铁0.2178.33%1732.58 二、焦碳0.613100.00%4904.24 禄丰冶金焦0.07712.64%619.84 贵机0.53687.36%4284.40 贵机0.0000.00% 三、动力 水5.0005.000 电4269.4394350.460 四、辅料0.500 铁矿0.0000.213 白云石0.000 硅石0.5000.5304240.00 电极糊0.0290.029232.00 元素MnFePSiC其它 合金成分65.20%15.07%0.250%17.50

43、%1.49%0.50% 回收率81.00%95.00%85.00%41.00%39.27% 综合样66.73%13.69%0.23%17.11%1.74%0.50% 综合样回收率81.50%98.70%80.41%38.40%4.12% 66.32%13.18%0.24%18.27% 工艺控制Mn/FeMn/PR3Mn/SiO3Mg/Al2O4S/A 理论值5.07273.680.700.880 实际值5.90286.280.8580.556.94 品种MnFePSiO2CaOMgO 平台块矿25.47%2.51%0.187%4.78%26.35%3.09% 澳矿高铁36.67%16.85%0

44、.071%9.30%0.00%1.81% 缅块矿 28.10%3.68%0.120%33.38%0.62%3.43% 碳锰球团27.58%4.75%0.136%13.27%6.60%3.39% 富锰渣外28.97%1.87%0.042%31.12%4.16%1.72% 南非低锰37.50%6.14%0.050%6.99%10.67%3.06% 4#矿28.24%5.15%0.130%27.86%10.50%3.95% 澳矿高锰45.70%5.62%0.060%13.79%0.00%2.00% 5#平台矿33.360%4.630%0.242%17.200%22.660%2.990% 混矿代入88

45、8.65126.732.92462.13300.4874.05 混矿成分30.79%4.39%0.101%16.01%10.41%2.57% 产 品 控 制 锰 矿 料 比 硅锰配料计算 混料代入888.65150.533.101036.28304.3082.09 混料成分25.90%4.39%0.09%30.21%8.87%2.39% 铁矿1.36%51.22%0.100%4.90%1.93%2.68% 白云石32.75%21.54% 硅石95.82% FeP 贵机（浩)78.27%18.98%2.75%9.10%11.47%0.13% 贵机77.82%18.38%3.80%8.60%19.

46、26%0.16% 贵机(贞）78.360%18.240%3.400%7.200%26.32%0.17% 混焦代入532.30126.4620.9260.3123.810.19 混焦成份78.32%18.61%3.08%8.15%18.82%0.15% 理论配碳 元素MnFeP SiO2CaOMgO 入渣率12.00%3.00%10.00%48.00%95.00%95.00% 入渣量106.644.520.31497.41289.0977.99 渣成分8.94%0.38%0.03%41.72%24.24%6.54% 锰 矿 料 比 熔 剂 焦 炭 炉 渣 392.57392.57 品种CAVW

47、合计批料产量80008000 100.00% 1085.291085.293821273.20721273.207 一、锰矿 其他 R初平台块矿 0.37澳矿高铁 0.37缅块矿 Al2O3CH2O配比 比例Mn/FeMn/PR3碳锰球团 0.58%7.20%80026.67%10.15136.206.16富锰渣外 1.55%0.51%2006.67%2.18516.480.19南非低锰 13.50%8.90%00.00%7.64234.170.124#矿 4.00%3.90%3.00%45015.00%5.81202.790.75澳矿高锰 10.95%1.00%86028.67%15.496

48、89.760.195#平台矿 0.40%5.60%30010.00%6.11750.001.96二、焦碳 0.30%0.80%1003.33%5.48217.230.52贵机（浩) 1.55%5.42%2909.67%8.13761.670.15贵机 0.45%0.450%00.00%7.21137.851.49贵机(贞） 123.7617.02114.0430001.00三、动力 4.29%0.59%3.80%水 成本项目 砚山富锰渣 新澳矿 1澳矿高铁 备用 149.3717.02119.213550电 4.35%0.50%3.36%四、辅料 1.13%3.98%0铁矿 0.40%0白云石

49、 0.94%550硅石 电极糊 SiO2CaOMgOAl2O3 比例 五、工资 50.05%2.55%6.86%20.25%37050.00%370六、制造费用 39.29%4.95%4.33%20.25%00.00%合 计 32.17%3.50%5.84%20.25%37050.00% 52.103.828.0425.61740592162 41.20%3.02%6.35%20.25%450148139.32 299.7 Al2O3 150.3 97.00% 144.891120.841192.38 12.15% R3=0.74 合计渣量 配比 灰份成份 546 2.6592.3000.8190.7733,138.242,801.6321273.21#REF! 234.50234.50 2,000.000.6840.6130.1740.206348.46412.275472.44#REF! 4,0