10吨edi超纯水设备设计方案

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1、10m³EDI超纯水设备设计方案一、EDI超纯水设备设计依据及处理水标准：1.EDI超纯水设备设计依据：1.1原水：自来水　　1.2产水用途：锅炉用水　　1.3产水量：RO出水水量≥13.5m3/h；EDI出水水量≥10.0m3/h　　1.4出水水质：出水电阻率≥10MΩ.CM；终端出水电阻率≥17MΩ.CM　　1.5系统配置：预处理+反渗透除盐+EDI精除盐　　1.6运行方式：自动控制运行　　1.7设计界线：从原水箱出口至用水点(详见工艺流程图)　　1.8设备工艺参数满足《工业用水软化除盐设计规范》(GBJ109-87)；　　1.9设备安装调试满足《给水排水工程施工验收规范》(GB132

2、8-1995)。　　1.10其他涉及的设计基础条件将在技术讨论中确定2、EDI超纯水设备系统对外界要求：2.1进水管：进水管接至原水箱入口。　　2.2供电缆：根据算出的容量，用户将动力电分别送至操作控电控柜上。　　2.3出水管：至用水点。(详见工艺流程图)。　　2.4地基要求：地基承载力≥5吨/平方　　2.5废水处理：排至厂房内地沟(用户考虑)。　　2.6系统水温：常温。　　2.7占地面积：30平方米，L*B=6*5。[键入文字]5广州昌硕环保设备有限公司二、EDI超纯水设备工艺流程示意图(如图)：还原剂絮凝剂阻垢剂原水箱保安过滤器2007年河西水厂原水水质检验报告项目单位1.92.14.

3、55.146.47.98.19.1110.911.512.10水温℃1818203030313028302422电导率10060110180155130110107126145140砷mg/l0.000780.000420.001080.001040.000940.001000.000960.000300.00060汞mg/l0.0000200.0000200.0000360.0000240.0000200.0000200.0000200.0000200.0000200.0000220.000058镉mg/l0.000090.000090.000090.000090.000090.0000

4、90.000090.000120.00009铬六价mg/l0.0040.0040.0040.0040.0040.0040.0040.0040.0040.0040.004铅mg/l0.00090.00090.00090.00340.00090.00090.00090.00120.0009硒mg/l0.000080.000160.000080.000450.000080.000080.000080.000340.00008氰化物mg/l0.0040.0040.0040.0040.0040.004-0.0010.0040.0040.0040.004Ph值mg/l7.607.207.106.846

5、.987.247.117.176.927.286.93溶解氧mg/l8.769.408.336.447.027.176.746.865.896.836.08高锰酸盐指数mg/l3.51.22.43.93.33.22.93.63.24.04.5BOD5mg/l0.270.250.911.361.182.091.981.120.382.821.50氨氮mg/l0.370.050.160.40.210.580.200.310.210.420.43粪大肠杆菌群mg/l40033001400900900170001400200790013001400总磷mg/l0.040.020.070.070.0

6、70.060.050.070.090.080.09氟化物mg/l0.170.060.180.370.250.200.200.180.160.200.26挥发酚mg/l0.0020.0020.0020.0020.0020.0020.0020.0020.0020.0020.002硫酸盐mg/l9.363.3811.1017.8114.9214.4011.1410.3611.2015.8615.32氯化物mg/l5.452.186.3710.709.168.467.206.606.368.557.84硝酸盐氮mg/l1.440.401.383.382.682.341.321.901.582.12

7、1.94铁mg/l0.300.1340.2870.5290.2780.5180.4720.4440.3620.6320.527锰mg/l0.0360.0080.0540.1420.0570.0790.0820.0580.0500.1250.111铜mg/l0.00330.00080.00130.00240.00410.00100.00190.00140.0121锌mg/l0.0080.0090.0080.0080.008