1#炉碳锰配料 (4).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68.00%91.50%85.00%2.77% 综合样65.54%25.86%0.55%1.06%6.49%0.50%100.00% 综合样回收率66.44%96.94%82.16%4.84%15.91% 理论合金成分67.08%24.41%0.57%0.61%6.93% 工艺控制Mn/FeMn/PR3Mn/SiO3Mn/Al2O4A/SMn/MgO 理论值3.37160.291.50 实际值3.70147.371.562.107.250.297.47 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% 富锰渣外27.06%2.30%0.050%27.91%6.06%0.75%11.36% 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%

3、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% 金隆水洗 矿 27.560%9.100%0.162%19.500%0.360%1.810% 混矿代入296.3742.511.92129.38178.6537.1335.50 混矿成分30.63%4.39%0.198%13.37%18.47%3.84%3.67% 混料代入297.2880.392.02141.56180.8839.7741.02 混料成分29.03%7.85%0.20%13.82%17.66%3.88

4、%4.01% 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 冶金焦77.91%18.77%3.32%8.60%8.00%0.16%49.85% 省内焦79.16%17.40%3.44%13.00%6.67%0.14%54.04% 贵机77.957%19.653%2.389%7.463%19.26%0.16%39.29% 混焦代入85.5920.912.8910.623.460.038.89 混焦成份78.24%19.12%2.64%8.85%16.53%0.15%42.49% 理论配碳 元素MnFePSiO

5、2CaOMgOAl2O3 入渣率27.00%5.00%10.00%88.00%95.00%95.00%95.00% 入渣量80.274.020.20124.57171.8437.7838.97 渣成分15.64%0.78%0.04%24.27%33.48%7.36%7.59% 产 品 控 制 122.93122.93 锰 矿 料 比 熔 剂 焦 炭 品种CA 炉 渣 VW 灰份成份 批料产量 301.35 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%6002.5406.8441.42260.0%3#炉回炉渣 8.375%1604

6、.3299.2471.42916.0%碳锰球团 0.542%01.4916.5211.4870.0%缅块矿 0.89%0.24411.7655.4120.0%南非低锰 0.100%0.2435.17867.4830.0%金隆水洗矿 3.30%4.111%1100.5685.2152.16711.0%二、焦碳 8.900%1300.1227.6362.48713.0%冶金焦 1.20%2.2446.0627.3390.0%省内焦 0.500%0.1113.0291.7010.0%贵机 3.4832.5610001.6686.9721.545三、动力 0.36%3.26%1.6686.9721.5

7、45水 3.4845.9610701.5593.6981.474电 0.34%4.30%1.5593.6981.474四、辅料 3.978%700.9420.0270.136铁矿 0.50%0硅石 0水洗碎铁 电极糊 CaOMgOAl2O3五、工资 8.69%2.77%28.02%00.0% 六、制造费用 2.71%3.00%31.73%3025.0%合 计 4.95%4.33%20.25%9075.0% 0.930.844.76120 4.46%4.04%22.74% 482.41513.20 R3=1.68 成本项目 配比比例 172.35 合计渣量 灰份成份 #3.2102.6600.9

8、830.8123,039.932,508.13#REF!#REF! 199.34199.34 3,130.001.9811.5960.6540.5272,046.021,648.51#REF!#REF! 2,000.000.4860.4260.1310.115262.70229.82#REF!#REF! 2,810.000.0000.0000.0000.0000.000.00#REF!#REF! 3,880.000.0000.0000.0000.0000.000.00#REF!#REF! 21.490.0000.0000.0000.0000.000.00#REF!#REF! 3,517.000

9、.3500.2930.0880.074309.47258.71#REF!#REF! 3,819.000.3930.3460.1100.097421.74371.09#REF!#REF! 4,780.000.0000.0000.0000.0000.000.00#REF!#REF! 1,200.000.0000.0000.0000.0000.000.00#REF!#REF! 1,902.840.3630.497690.68945.54#REF! 1,970.000.0000.0000.000.00#REF!#REF! 1,880.000.0870.124162.83233.59#REF!#REF!

10、 1,910.000.2760.373527.86711.95#REF!#REF! 1,473.951,346.54#REF! 2.503.5003.4008.758.50#REF!#REF! 0.443330.0003041.0001,465.201,338.04#REF!#REF! 0.232253.21292.60#REF! 660.000.2320.280153.31184.80#REF!#REF! 190.000.0000.000.00#REF!#REF! 0.0000.000.00#REF!#REF! 3,850.000.0280.02899.90107.80#REF!#REF!

11、141.79141.79#REF! 六、制造费用209.11209.11#REF! 5,964.00-44.008320.9446,008.015,643.06#REF! 计划总成 本 （元） 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) 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72.00%88.00%85.00%2.66% 综合样65.54%

12、25.86%0.55%1.06%6.49%0.50%100.00% 综合样回收率70.78%91.69%88.70%4.64%16.00% 理论合金成分66.67%24.82%0.53%0.61%6.90% 工艺控制Mn/FeMn/PR3Mn/SiO3Mn/Al2O4A/SMn/MgO 理论值3.06151.391.50 实际值3.28149.341.351.896.190.317.30 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

13、.070%3.770%0.58% 5#平台矿32.410%4.970%0.218%17.200%22.660%2.990%0.45% 富锰渣外27.06%2.30%0.050%27.91%6.06%0.75%11.36% 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%0.056%4.72%9.24%1.35%0.57% 金隆水洗

14、矿 27.560%9.100%0.162%19.500%0.360%1.810% 混矿代入296.1541.791.86141.91169.3337.3241.18 混矿成分30.00%4.23%0.189%14.38%17.15%3.78%4.17% 混料代入297.3290.561.99157.18172.2040.7148.01 混料成分28.03%8.54%0.19%14.82%16.23%3.84%4.53% 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 冶金焦77.91%18.77%3.32%8

15、.60%8.00%0.16%49.85% 省内焦79.16%17.40%3.44%13.00%6.67%0.14%54.04% 贵机77.957%19.653%2.389%7.463%19.26%0.16%39.29% 混焦代入107.2326.363.5512.864.510.0411.03 混焦成份78.19%19.22%2.59%8.57%17.09%0.15%41.83% 理论配碳 元素MnFePSiO2CaOMgOAl2O3 入渣率23.00%5.00%10.00%88.00%95.00%95.00%95.00% 入渣量68.384.530.20138.31163.5938.6845

16、.61 渣成分13.37%0.89%0.04%27.04%31.99%7.56%8.92% 产 品 控 制 130.27130.27 锰 矿 料 比 熔 剂 焦 炭 品种CA 炉 渣 VW 灰份成份 批料产量 321.09 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%5002.5406.8441.42250.0%3#炉回炉渣 8.375%2204.3299.2471.42922.0%碳锰球团 0.542%01.4916.5211.4870.0%缅块矿 0.89%0.24411.7655.4120.0%南非低锰 0.100%0.2

17、435.17867.4830.0%金隆水洗矿 3.30%4.111%1200.5685.2152.16712.0%二、焦碳 8.900%1900.1227.6362.48719.0%冶金焦 1.20%2.2446.0627.3390.0%省内焦 0.500%0.1113.0291.7010.0%贵机 3.8042.8210301.4567.0871.589三、动力 0.38%4.16%1.4567.0871.589水 3.8059.2611201.3553.2831.493电 0.36%5.29%1.3553.2831.493四、辅料 3.978%900.9420.0270.136铁矿 0.5

18、0%0硅石 0水洗碎铁 电极糊 CaOMgOAl2O3五、工资 8.69%2.77%28.02%00.0% 六、制造费用 2.71%3.00%31.73%3020.0%合 计 4.95%4.33%20.25%12080.0% 1.201.085.86150 4.56%4.10%22.23% 480.76511.45 R3=1.46 成本项目 配比比例 182.24 合计渣量 灰份成份 #3.0742.6600.9220.8192,834.572,514.36#REF!#REF! 199.34199.34 3,130.001.5491.3300.5110.4391,600.211,373.76#

19、REF!#REF! 2,000.000.6280.5850.1700.158339.00316.01#REF!#REF! 2,810.000.0000.0000.0000.0000.000.00#REF!#REF! 3,880.000.0000.0000.0000.0000.000.00#REF!#REF! 21.490.0000.0000.0000.0000.000.00#REF!#REF! 3,517.000.3580.3190.0900.080316.86282.23#REF!#REF! 3,819.000.5390.5050.1510.142578.50542.36#REF!#REF!

20、 4,780.000.0000.0000.0000.0000.000.00#REF!#REF! 1,200.000.0000.0000.0000.0000.000.00#REF!#REF! 1,904.290.4270.497813.37946.29#REF! 1,970.000.0000.0000.000.00#REF!#REF! 1,880.000.0810.099152.82186.87#REF!#REF! 1,910.000.3460.398660.55759.42#REF!#REF! 1,473.951,346.54#REF! 2.503.5003.4008.758.50#REF!#

21、REF! 0.443330.0003041.0001,465.201,338.04#REF!#REF! 0.280284.90292.60#REF! 660.000.2800.280185.00184.80#REF!#REF! 190.000.0000.000.00#REF!#REF! 0.0000.000.00#REF!#REF! 3,850.000.0280.02899.90107.80#REF!#REF! 141.79141.79#REF! 六、制造费用209.11209.11#REF! 5,964.006.979313.9745,957.025,650.03#REF! 计划总成 本 （

22、元） 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) 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77.00%91.50%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76.66%92.23%93.29%5.20%16.05% 理论合金成分65.83%25.66%0.50%0

23、.61%6.87% 工艺控制Mn/FeMn/PR3Mn/SiO3Mn/Al2O4A/SMn/MgO 理论值2.98141.561.50 实际值3.05145.021.451.966.500.307.25 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% 富锰渣外27.06%2.30%0.050%27.91%

24、6.06%0.75%11.36% 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%0.056%4.72%9.24%1.35%0.57% 金隆水洗 矿 27.560%9.100%0.162%19.500%0.360%1.810% 混矿代入295.5842.561.90132.34174.8936.9836.82 混矿成分30.57%4

25、.40%0.196%13.69%18.08%3.82%3.81% 混料代入296.8897.362.05151.56178.2640.9345.69 混料成分28.39%9.31%0.20%14.49%17.05%3.91%4.37% 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 冶金焦77.91%18.77%3.32%8.60%8.00%0.16%49.85% 省内焦79.16%17.40%3.44%13.00%6.67%0.14%54.04% 贵机77.957%19.653%2.389%7.463%19

26、.26%0.16%39.29% 混焦代入139.7634.124.7217.405.620.0514.52 混焦成份78.25%19.10%2.64%8.88%16.47%0.15%42.56% 理论配碳 元素MnFePSiO2CaOMgOAl2O3 入渣率18.00%5.00%10.00%88.00%95.00%95.00%95.00% 入渣量53.444.870.20133.38169.3538.8843.40 渣成分10.90%0.99%0.04%27.21%34.55%7.93%8.85% 产 品 控 制 140.41140.41 锰 矿 料 比 熔 剂 焦 炭 品种CA 炉 渣 VW

27、 灰份成份 批料产量 347.23 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%5902.5406.8441.42259.0%3#炉回炉渣 8.375%1504.3299.2471.42915.0%碳锰球团 0.542%01.4916.5211.4870.0%缅块矿 0.89%0.24411.7655.4120.0%南非低锰 0.100%0.2435.17867.4830.0%金隆水洗矿 3.30%4.111%1200.5685.2152.16712.0%二、焦碳 8.900%1400.1227.6362.48714.0%冶金焦

28、 1.20%2.2446.0627.3390.0%省内焦 0.500%0.1113.0291.7010.0%贵机 3.8032.9710001.6016.9451.556三、动力 0.39%3.30%1.6016.9451.556水 3.8054.3411001.4463.0491.450电 0.36%4.94%1.4463.0491.450四、辅料 3.978%1000.9420.0270.136铁矿 0.50%0硅石 0水洗碎铁 电极糊 CaOMgOAl2O3五、工资 8.69%2.77%28.02%00.0% 六、制造费用 2.71%3.00%31.73%5025.5%合 计 4.95%

29、4.33%20.25%14674.5% 1.521.387.78196 4.45%4.03%22.80% 460.73490.14 R3=1.56 成本项目 配比比例 196.91 合计渣量 灰份成份 #2.7852.6600.8510.8112,646.982,518.36#REF!#REF! 199.34199.34 3,130.001.6901.5690.5580.5181,746.081,621.03#REF!#REF! 2,000.000.3960.3990.1070.108213.74215.46#REF!#REF! 2,810.000.0000.0000.0000.0000.00

30、0.00#REF!#REF! 3,880.000.0000.0000.0000.0000.000.00#REF!#REF! 21.490.0000.0000.0000.0000.000.00#REF!#REF! 3,517.000.3310.3190.0830.080293.00282.23#REF!#REF! 3,819.000.3670.3720.1030.105394.17399.64#REF!#REF! 4,780.000.0000.0000.0000.0000.000.00#REF!#REF! 1,200.000.0000.0000.0000.0000.000.00#REF!#REF

31、! 1,902.690.5140.497978.67945.47#REF! 1,970.000.0000.0000.000.00#REF!#REF! 1,880.000.1250.127235.52238.36#REF!#REF! 1,910.000.3890.370743.15707.11#REF!#REF! 1,473.951,346.54#REF! 2.503.5003.4008.758.50#REF!#REF! 0.443330.0003041.0001,465.201,338.04#REF!#REF! 0.288289.97292.60#REF! 660.000.2880.28019

32、0.07184.80#REF!#REF! 190.000.0000.000.00#REF!#REF! 0.0000.000.00#REF!#REF! 3,850.000.0280.02899.90107.80#REF!#REF! 141.79141.79#REF! 六、制造费用209.11209.11#REF! 5,964.0024.187310.7955,939.815,653.20#REF! 计划总成 本 （元） 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

33、本（元 /t) 本月计划 消耗（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77.00%91.50%85.00%3.24% 综合样65.54%25.86%0.55%1.06%6.49%0.50%100.00% 综合样回收率76.54%92.59%92.82%5.66%16.08% 理论合金成分65.93%25.56%0.50%0.61%6.86% 工艺控制Mn/FeMn/PR3Mn/SiO3Mn/Al2O4A/SMn/MgO 理论值2.98141.561.50 实际值3.07144.511.472.1313.

34、050.167.84 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% 富锰渣外27.06%2.30%0.050%27.91%6.06%0.75%11.36% 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%16.25

35、1%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% 金隆水洗 矿 27.560%9.100%0.162%19.500%0.360%1.810% 混矿代入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274.5189.541.90128.75154.8535.0221.03 混料成分27.12%8.85%0

36、.19%12.72%15.30%3.46%2.08% 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 冶金焦77.91%18.77%3.32%8.60%8.00%0.16%49.85% 省内焦79.16%17.40%3.44%13.00%6.67%0.14%54.04% 贵机77.957%19.653%2.389%7.463%19.26%0.16%39.29% 混焦代入132.1532.434.4016.025.480.0513.63 混焦成份78.20%19.19%2.61%8.66%16.91%0.15%

37、42.04% 理论配碳 元素MnFePSiO2CaOMgOAl2O3 入渣率18.00%5.00%10.00%88.00%95.00%95.00%95.00% 入渣量49.414.480.19113.30147.1133.2719.98 渣成分12.11%1.10%0.05%27.76%36.05%8.15%4.90% 炉 渣 VW 灰份成份 129.35129.35 锰 矿 料 比 熔 剂 焦 炭 品种CA 产 品 控 制 批料产量 320.58 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%2602.5406.8441.422

38、26.0%3#炉回炉渣 8.375%4004.3299.2471.42940.0%碳锰球团 0.542%01.4916.5211.4870.0%缅块矿 0.89%0.24411.7655.4120.0%南非低锰 0.100%0.2435.17867.4830.0%金隆水洗矿 3.30%4.111%1200.5685.2152.16712.0%二、焦碳 8.900%0.1227.6362.4870.0%冶金焦 1.20%2.2446.0627.3390.0%省内焦 0.500%2200.1113.0291.70122.0%贵机 3.8040.8610001.6465.6241.536三、动力 0

39、.40%4.09%1.6465.6241.536水 3.8059.7510721.4753.0661.445电 0.38%5.57%1.4753.0661.445四、辅料 3.978%720.9420.0270.136铁矿 0.50%0硅石 0水洗碎铁 电极糊 CaOMgOAl2O3五、工资 8.69%2.77%28.02%00.0% 六、制造费用 2.71%3.00%31.73%4021.6%合 计 4.95%4.33%20.25%14578.4% 1.471.327.26185 4.53%4.08%22.39% 383.64408.13 R3=1.59 合计渣量 灰份成份 配比比例 181

40、.08 成本项目 #2.9922.6600.8530.7571,993.962,273.38#REF!#REF! 199.34199.34 3,130.000.8070.6920.2660.228833.43714.35#REF!#REF! 2,000.001.1431.0640.3090.287617.35574.56#REF!#REF! 2,810.000.0000.0000.0000.0000.000.00#REF!#REF! 3,880.000.0000.0000.0000.0000.000.00#REF!#REF! 21.490.0000.0000.0000.0000.000.00#

41、REF!#REF! 3,517.000.3590.3190.0900.080317.36282.23#REF!#REF! 3,819.000.0000.0000.0000.0000.000.00#REF!#REF! 4,780.000.0000.0000.0000.0000.000.00#REF!#REF! 1,200.000.6830.5850.1880.161225.82702.24#REF!#REF! 1,903.820.5270.4971,003.51946.05#REF! 1,970.000.0000.0000.000.00#REF!#REF! 1,880.000.1090.1072

42、04.08202.02#REF!#REF! 1,910.000.4190.390799.43744.02#REF!#REF! 1,473.951,346.54#REF! 2.503.5003.4008.758.50#REF!#REF! 0.443330.0003041.0001,465.201,338.04#REF!#REF! 0.225248.13292.60#REF! 660.000.2250.280148.23184.80#REF!#REF! 190.000.0000.000.00#REF!#REF! 0.0000.000.00#REF!#REF! 3,850.000.0280.0289

43、9.90107.80#REF!#REF! 141.79141.79#REF! 六、制造费用209.11209.11#REF! 5,964.00694.218555.1925,269.785,408.81#REF! 计划总成 本 （元） 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) 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77.00%91.50%

44、85.00%3.20% 综合样65.54%25.86%0.55%1.06%6.49%0.50%100.00% 综合样回收率76.95%91.34%93.18%5.60%16.09% 理论合金成分65.58%25.91%0.50%0.61%6.86% 工艺控制Mn/FeMn/PR3Mn/SiO3Mn/Al2O4A/SMn/MgO 理论值2.98141.561.50 实际值3.01144.311.552.109.280.237.40 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

45、%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% 富锰渣外27.06%2.30%0.050%27.91%6.06%0.75%11.36% 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%0.056%4.72%

46、9.24%1.35%0.57% 金隆水洗 矿 27.560%9.100%0.162%19.500%0.360%1.810% 混矿代入275.1843.091.78113.89163.4633.7621.57 混矿成分28.84%4.52%0.187%11.94%17.13%3.54%2.26% 混料代入276.3391.851.91131.66166.5637.3529.79 混料成分27.02%8.98%0.19%12.88%16.29%3.65%2.91% 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

47、冶金焦77.91%18.77%3.32%8.60%8.00%0.16%49.85% 省内焦79.16%17.40%3.44%13.00%6.67%0.14%54.04% 贵机77.957%19.653%2.389%7.463%19.26%0.16%39.29% 混焦代入132.1532.434.4016.025.480.0513.63 混焦成份78.20%19.19%2.61%8.66%16.91%0.15%42.04% 理论配碳 元素MnFePSiO2CaOMgOAl2O3 入渣率18.00%5.00%10.00%88.00%95.00%95.00%95.00% 入渣量49.744.590.

48、19115.86158.2335.4828.30 渣成分11.45%1.06%0.04%26.66%36.42%8.17%6.51% 产 品 控 制 130.90130.90 锰 矿 料 比 熔 剂 焦 炭 品种CA 炉 渣 VW 灰份成份 批料产量 324.43 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%3102.5406.8441.42231.0%3#炉回炉渣 8.375%4004.3299.2471.42940.0%碳锰球团 0.542%01.4916.5211.4870.0%缅块矿 0.89%0.24411.7655.

49、4120.0%南非低锰 0.100%0.2435.17867.4830.0%金隆水洗矿 3.30%4.111%1200.5685.2152.16712.0%二、焦碳 8.900%600.1227.6362.4876.0%冶金焦 1.20%2.2446.0627.3390.0%省内焦 0.500%1100.1113.0291.70111.0%贵机 3.8045.9110001.7326.3861.545三、动力 0.40%4.59%1.7326.3861.545水 3.8065.4310881.5493.0081.443电 0.37%6.01%1.5493.0081.443四、辅料 3.978%880.9420.0270.136铁矿 0.50%0硅石 0水洗碎铁 电极糊 CaOMgOAl2O3五、工资 8.69%2.77%28.02%00.0% 六、制造费用 2.71%3.00%31.73%4021.6%合 计 4.95%4.33%20.25%14578.4% 1.471.327.26185 4.53%4.08%22.39% 408.43434.50 R3=1.67 成本项目 配比比例 183.25 合计渣量 灰份成份 #2.9412.6600.8480.7652,197.8