污染物排放量计算公式

1、垃圾系数人数 天数垃圾量0.547030011.34排放浓度排放量清洗废水cod2000.03072153.6：SS150：0.02304循环废水SS300全盐量投入物料1输液袋碎料(pvc4903.5512输液瓶碎料(PP1961.4223PVC碎屑34PP碎屑45黑色母料14056677总计7004.9711气量产生浓度mg/m产量t/a风量m3/h时间h集气效率收集量t非甲烷2.4E+08333.33331003000080000.880720000200014.4300024001人数定濒1/人用水量废水量m3匕粪池CO浓度氨氮浓度cod量7035735153.6350350.0537

2、6颗粒物非甲烷0.9PF原料破碎热熔:颗粒1961.421961.421961.421960.55碎屑0.03非甲烷1.9PV(原料破碎热熔:颗粒4903.554903.554903.554901.73碎屑0.08纸屑废橡胶cod量cod系数1.094104223.2PVC0.080.25原料清洗甩干风选4901.94901.94901.822.749369cod量cod系数1.655265844.2纸屑废橡胶PP0.020.1原料清洗甩干风选1960.751960.751960.73原材料t水残留比例残留水量t葡萄糖浓度6862.650.13.430.8cod 量t匍萄糖量t葡萄糖浓度;残留

3、水量t0.2880.2699156526.9915651原材料t水残留比例残留水量t盐浓度6862.650.13.430.6cod 量t匍萄糖量t葡萄糖浓度1残留水量t0.040.044粉尘 气量m3/h年工作时间总气量m3/a氮氧化物6390720046008000 烟尘PV（管 道5000PP管道2000颗粒物0非甲烷总烃4.9总计7004.9产出物料产污系数原料量产牛量废气6240.281062402.8烟尘37.6100.376产生浓度6025.370656so2nox去除效率有!组织排放t/a扌电放浓度mg/m3无组织t/a截留t/a排放速率kg/0.990.83.333333332

4、079.20.41666741.6666780活性炭0.9264343.2氨氮量一级bcod浓度-级b氨氮浓度出水COD出水氨氮0.005376400350.061440.00537650500排放浓度排放量1000.0310000.30.02非甲烷切割碎屑0.50.03热熔挤塑切割管道1960.551960.052000.052000母料400.05非甲烷切割碎屑1.60.08热熔挤塑切割管道4901.734900.135000.135000母料100残留塑料切割粉尘0.150.05粉尘非甲烷非甲烷切割碎屑0.020.80.70.5粉碎热熔造粒挤塑切割产品4901.574902.24901.

5、255000.555000碎屑母料0.65100残留塑料切割粉尘0.060.02粉尘非甲烷非甲烷切割碎屑0.010.40.20.2粉碎热熔造粒挤塑切割产品1960.631960.881960.422000.2212000碎屑母料0.2640匍萄糖量tcod 量t清洗水tcod 浓度 mg/l0.027440.02927848153.6)190.6151042原料量t残留比例6862.650.393311114盐量tcod 量t清洗水tcod 浓度 mg/l0.020580.02058153.6133.984375原料量t残留比例6862.650.058286522排放浓度 排放量t/a12.370.56911896134.84464249.68928487.50.345060.69012天然气用量废气量640000 9600000nox量nox浓度s