除盐水站计算表

除盐水计算：,,,,,,,

进水水质,阳离子,Na+=,0.5,meq/L,,,

,,Ca2+=,1,meq/L,CK=,2,meq/L

,,Mg2+=,0.5,meq/L,,,

,阴离子,HCO-=,1.36,meq/L,,,

,,SO42-=,0.5,meq/L,CA=,2,meq/L

,,Cl-=,0.14,meq/L,,,

,二氧化硅,SiO2=,15,mg/L,,,

,总硬度,H0=,1.5,meq/L,,,

,温度,Td=,20,℃,,,

成品水,含盐量（小于）,,,5.000,mg/L,,

要求,电导率（小于）,,,10.000,μΩ/cm,,

,二氧化硅（小于）,,SiO2=,100.000,μg/L,,

,钠(阳床出水小于),,Na+=,100.000,μg/L,,

处理能力,设计要求产水量,,Q0=,200.000,m3/h,,

,运行周期,,Th=,20.000,h,,

,再生历时,,th1=,4.000,h,,

参数,进入阴床总阴离子量,,CA0=,1.004,meq/L,,

,阳树脂标准工作交换容量,,EK0=,900.000,eq/m3树脂,,

的选定,阳树脂设计工作交换容量,,EK=,850.000,eq/m3树脂,,

,阴树脂标准工作交换容量,,EA0=,250.000,eq/m3树脂,,

和计算,阴树脂设计工作交换容量,,EA=,250.000,eq/m3树脂,,

,自用水率计算系数,,aK1=,0.610,,,

,,,bK1=,0.770,,,

,,,aA1=,0.880,,,

,,,bA1=,0.990,,,

,阳交换柱再生自用除盐水率,,NK1=,0.011,,,

,阴交换柱再生自用除盐水率,,NA1=,0.009,,,

,系统自用除盐水率,,N1=,0.020,,,

,自用水率计算系数,,aK2=,1.540,,,

,,,bK2=,0.560,,,

,,,aA2=,2.770,,,

,,,bA2=,0.960,,,

,阳交换柱再生自用清水率,,NK2=,0.024,,,

,阴交换柱再生自用清水率,,NA2=,0.028,,,

,系统自用清水率,,N2=,0.052,,,

,阴交换柱产水量,,QA=,203.969,m3/h,,

,阳交换柱产水量,,QK=,203.969,m3/h,,

,进水需用量,,QS=,214.542,m3/h,,

,串联系统阴树脂富裕系数,,a=,0.100,,,

,阴、阳树脂体积比,,RV=,0.533,,,

,运行设备考虑套数,,n=,3.000,套,,

,每套设备产水量,,Q'=,66.667,m3/h,,

,每套阴交换柱产水量,,Q'A=,67.990,m3/h,,

,每套阳交换柱产水量,,Q'K=,67.990,m3/h,,

,每套设备进水需用量,,Q'S=,71.514,m3/h,,

阳交换柱,运行流量,,QK1=,81.588,m3/h,,

的选择,直径,,DK1=,2500.000,mm,,

,截面积,,FK1=,4.909,m2,,

,运行速度,,WK1=,16.621,m/h,,

,树脂体积,,VK1=,3.839,m3,,

,树脂高度,,hK1=,0.782,m,,

,实际树脂高度,,hK2=,1.600,m,,

,实际树脂体积,,VK2=,7.854,m3,,

阳交换柱,实际运行周期,,TKj=,45.095,h,,

的运行参,实际运行流量,,QKj=,74.021,m3/h,,

数,实际运行流速,,WKj=,15.079,m/h,,

阳交换柱,再生剂种类,,盐酸(HCl),,,,

再生系统,再生剂用量,,LK=,45.000,Kg/m3树脂,,

参数计算,再生剂比耗,,n=,1.400,,,

,100%盐酸再生一次用量,,Gk=,353.429,kg,,

,工业用盐酸浓度,,Cy=,30.000%,,,

,工业用盐酸再生一次用量,,GKg=,1178.097,kg,,

,工业用盐酸比重,,γHg=,1.149,g/cm3,,

,再生液浓度,,Cyk=,0.020,,,

,再生液比重,,γHk=,1.008,g/cm3,,

,再生液体积,,VH=,17.531,m3,,

,配酸稀释用水量,,VH1=,16.506,m3,,

,再生液流速,,WH=,5.00,m/h,,

,进再生液时间,,tz=,42.86,min,,

,置换时间,,tK3=,25.00,min,,

,置换流速,,WK3=,5.00,m/h,,

,置换用水量,,VK03=,10.23,m3,,

,小反洗流速,,WK01=,15.00,m/h,,

,小反洗时间,,tK1=,10.00,min,,

,小反洗用水量,,VK01=,12.27,m3/h,,

,小正洗时间,,tK4=,15.00,min,,

,小正洗流速,,WK04=,15.00,m/h,,

,小正洗用水量,,VK04=,18.41,m3/h,,

,正洗时间,,tK5=,20.00,min,,

,正洗流速,,WK05=,10.00,m/h,,

,正洗用水量,,VK05=,16.36,m3/h,,

,大反洗时间,,tK2=,15.00,min,,

,大反洗流速,,WK02=,15.00,m/h,,

,大反洗用水量,,VK02=,18.41,m3/h,,

,顶压空气压力,,,0.3~0.5,kg/cm3,,

,顶压空气用量,,W1=,1.47,,,

二氧化碳,进水二氧化碳含量,,Cc1=,60.51,mg/L,,

器的选择,出水二氧化碳含量,,Cc2=,5.00,mg/L,,

,出二氧化碳总量,,Gc1=,11.32,kg/h,,

,出二氧化碳平均推动力,,⊿Cop=,0.02,kg/m3,,

,预选淋水密度,,q01=,60.00,m3/m2.h,,

,需工作断面积,,Fc01=,3.40,m2,,

,解吸系数,,Kc1=,0.35,m/h,,

,需填料工作面积,,Fc02=,1313.12,m2,,

,填料表面积,,S=,190.00,m2,,

,需填料体积,,Vc1=,6.91,m3,,

,需填料高度,,Hc1=,2.03,m,,

,台数,,nc=,2.00,台,,

,选型直径,,Dc1=,1500.00,mm,,

,实际断面积,,Fc0j=,3.53,m2,,

,实际淋水密度,,q0j=,57.71,m3/m2.h,,

,实际需填料高度,,Hcj=,2.04,m,,

,实际需填料体积,,Vcj=,7.22,m3,,

,需气水比,,mc=,25.00,m3/m3H2O,,

,需鼓气量,,Wq=,5099.23,m3/h,,

,需鼓风机风压,,Pf=,121.76,m,,

,风机型号,,,,,,

阴交换柱,运行流量,,QA1=,74.021,m3/h,,

,树脂体积,,VA=,14.740,m3,,

,计算运行周期,,TA=,49.604,h,,

的选择,直径,,DA1=,3000.000,mm,,

,截面积,,FA1=,7.069,m2,,

,计算高度,,hA=,2.085,m,,

,实际树脂高度,,hA2=,2.000,m,,

,实际树脂体积,,VA2=,14.137,m3,,

阴交换柱,实际运行周期,,TAj=,47.574,h,满足,

的运行参,实际运行流量,,QAj=,74.021,m3/h,,

数,实际运行流速,,WAj=,10.472,m/h,,

阴交换柱,再生剂种类,,烧碱（NaOH),,,,

再生系统,再生剂用量,,LA=,15.000,Kg/m3树脂,,

参数计算,再生剂比耗,,nA=,1.500,,,

,100%碱再生一次用量,,GA=,212.058,Kg,,

,工业用碱浓度,,Cji=,31.000%,,,

,工业用碱再生一次用量,,GAg=,684.056,Kg,,

,工业用碱比重,,γOHg=,1.340,g/cm3,,

,再生液浓度,,COHA=,0.020,,,

,再生液比重,,γOHA=,1.021,g/cm3,,

,再生液体积,,VOH=,10.385,m3,,

,配酸稀释用水量,,VOH1=,9.874,m3,,

,再生液流速,,WOH=,3.00,m/h,,

,进再生液时间,,tzA=,29.38,min,,

,置换时间,,tA3=,35.00,min,,

,置换流速,,WA3=,3.00,m/h,,

,置换用水量,,VA03=,12.37,m3,,

,小反洗流速,,WA01=,10.00,m/h,,

,小反洗时间,,tA1=,15.00,min,,

,小反洗用水量,,VA01=,17.67,m3/h,,

,小正洗时间,,tA4=,15.00,min,,

,小正洗流速,,WA04=,15.00,m/h,,

,小正洗用水量,,VA04=,26.51,m3/h,,

,正洗时间,,tA5