除鹽水站計算表

除鹽水計算：,,,,,,,

進水水質(zhì),陽離子,Na+=,0.5,meq/L,,,

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

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

,陰離子,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,,,

,總硬度,H0=,1.5,meq/L,,,

,溫度,Td=,20,℃,,,

成品水,含鹽量（小于）,,,5.000,mg/L,,

要求,電導(dǎo)率（小于）,,,10.000,μΩ/cm,,

,二氧化硅（小于）,,SiO2=,100.000,μg/L,,

,鈉(陽床出水小于),,Na+=,100.000,μg/L,,

處理能力,設(shè)計要求產(chǎn)水量,,Q0=,200.000,m3/h,,

,運行周期,,Th=,20.000,h,,

,再生歷時,,th1=,4.000,h,,

參數(shù),進入陰床總陰離子量,,CA0=,1.004,meq/L,,

,陽樹脂標準工作交換容量,,EK0=,900.000,eq/m3樹脂,,

的選定,陽樹脂設(shè)計工作交換容量,,EK=,850.000,eq/m3樹脂,,

,陰樹脂標準工作交換容量,,EA0=,250.000,eq/m3樹脂,,

和計算,陰樹脂設(shè)計工作交換容量,,EA=,250.000,eq/m3樹脂,,

,自用水率計算系數(shù),,aK1=,0.610,,,

,,,bK1=,0.770,,,

,,,aA1=,0.880,,,

,,,bA1=,0.990,,,

,陽交換柱再生自用除鹽水率,,NK1=,0.011,,,

,陰交換柱再生自用除鹽水率,,NA1=,0.009,,,

,系統(tǒng)自用除鹽水率,,N1=,0.020,,,

,自用水率計算系數(shù),,aK2=,1.540,,,

,,,bK2=,0.560,,,

,,,aA2=,2.770,,,

,,,bA2=,0.960,,,

,陽交換柱再生自用清水率,,NK2=,0.024,,,

,陰交換柱再生自用清水率,,NA2=,0.028,,,

,系統(tǒng)自用清水率,,N2=,0.052,,,

,陰交換柱產(chǎn)水量,,QA=,203.969,m3/h,,

,陽交換柱產(chǎn)水量,,QK=,203.969,m3/h,,

,進水需用量,,QS=,214.542,m3/h,,

,串聯(lián)系統(tǒng)陰樹脂富裕系數(shù),,a=,0.100,,,

,陰、陽樹脂體積比,,RV=,0.533,,,

,運行設(shè)備考慮套數(shù),,n=,3.000,套,,

,每套設(shè)備產(chǎn)水量,,Q'=,66.667,m3/h,,

,每套陰交換柱產(chǎn)水量,,Q'A=,67.990,m3/h,,

,每套陽交換柱產(chǎn)水量,,Q'K=,67.990,m3/h,,

,每套設(shè)備進水需用量,,Q'S=,71.514,m3/h,,

陽交換柱,運行流量,,QK1=,81.588,m3/h,,

的選擇,直徑,,DK1=,2500.000,mm,,

,截面積,,FK1=,4.909,m2,,

,運行速度,,WK1=,16.621,m/h,,

,樹脂體積,,VK1=,3.839,m3,,

,樹脂高度,,hK1=,0.782,m,,

,實際樹脂高度,,hK2=,1.600,m,,

,實際樹脂體積,,VK2=,7.854,m3,,

陽交換柱,實際運行周期,,TKj=,45.095,h,,

的運行參,實際運行流量,,QKj=,74.021,m3/h,,

數(shù),實際運行流速,,WKj=,15.079,m/h,,

陽交換柱,再生劑種類,,鹽酸(HCl),,,,

再生系統(tǒng),再生劑用量,,LK=,45.000,Kg/m3樹脂,,

參數(shù)計算,再生劑比耗,,n=,1.400,,,

,100%鹽酸再生一次用量,,Gk=,353.429,kg,,

,工業(yè)用鹽酸濃度,,Cy=,30.000%,,,

,工業(yè)用鹽酸再生一次用量,,GKg=,1178.097,kg,,

,工業(yè)用鹽酸比重,,γHg=,1.149,g/cm3,,

,再生液濃度,,Cyk=,0.020,,,

,再生液比重,,γHk=,1.008,g/cm3,,

,再生液體積,,VH=,17.531,m3,,

,配酸稀釋用水量,,VH1=,16.506,m3,,

,再生液流速,,WH=,5.00,m/h,,

,進再生液時間,,tz=,42.86,min,,

,置換時間,,tK3=,25.00,min,,

,置換流速,,WK3=,5.00,m/h,,

,置換用水量,,VK03=,10.23,m3,,

,小反洗流速,,WK01=,15.00,m/h,,

,小反洗時間,,tK1=,10.00,min,,

,小反洗用水量,,VK01=,12.27,m3/h,,

,小正洗時間,,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,,

,正洗時間,,tK5=,20.00,min,,

,正洗流速,,WK05=,10.00,m/h,,

,正洗用水量,,VK05=,16.36,m3/h,,

,大反洗時間,,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,,

,頂壓空氣壓力,,,0.3~0.5,kg/cm3,,

,頂壓空氣用量,,W1=,1.47,,,

二氧化碳,進水二氧化碳含量,,Cc1=,60.51,mg/L,,

器的選擇,出水二氧化碳含量,,Cc2=,5.00,mg/L,,

,出二氧化碳總量,,Gc1=,11.32,kg/h,,

,出二氧化碳平均推動力,,⊿Cop=,0.02,kg/m3,,

,預(yù)選淋水密度,,q01=,60.00,m3/m2.h,,

,需工作斷面積,,Fc01=,3.40,m2,,

,解吸系數(shù),,Kc1=,0.35,m/h,,

,需填料工作面積,,Fc02=,1313.12,m2,,

,填料表面積,,S=,190.00,m2,,

,需填料體積,,Vc1=,6.91,m3,,

,需填料高度,,Hc1=,2.03,m,,

,臺數(shù),,nc=,2.00,臺,,

,選型直徑,,Dc1=,1500.00,mm,,

,實際斷面積,,Fc0j=,3.53,m2,,

,實際淋水密度,,q0j=,57.71,m3/m2.h,,

,實際需填料高度,,Hcj=,2.04,m,,

,實際需填料體積,,Vcj=,7.22,m3,,

,需氣水比,,mc=,25.00,m3/m3H2O,,

,需鼓氣量,,Wq=,5099.23,m3/h,,

,需鼓風(fēng)機風(fēng)壓,,Pf=,121.76,m,,

,風(fēng)機型號,,,,,,

陰交換柱,運行流量,,QA1=,74.021,m3/h,,

,樹脂體積,,VA=,14.740,m3,,

,計算運行周期,,TA=,49.604,h,,

的選擇,直徑,,DA1=,3000.000,mm,,

,截面積,,FA1=,7.069,m2,,

,計算高度,,hA=,2.085,m,,

,實際樹脂高度,,hA2=,2.000,m,,

,實際樹脂體積,,VA2=,14.137,m3,,

陰交換柱,實際運行周期,,TAj=,47.574,h,滿足,

的運行參,實際運行流量,,QAj=,74.021,m3/h,,

數(shù),實際運行流速,,WAj=,10.472,m/h,,

陰交換柱,再生劑種類,,燒堿（NaOH),,,,

再生系統(tǒng),再生劑用量,,LA=,15.000,Kg/m3樹脂,,

參數(shù)計算,再生劑比耗,,nA=,1.500,,,

,100%堿再生一次用量,,GA=,212.058,Kg,,

,工業(yè)用堿濃度,,Cji=,31.000%,,,

,工業(yè)用堿再生一次用量,,GAg=,684.056,Kg,,

,工業(yè)用堿比重,,γOHg=,1.340,g/cm3,,

,再生液濃度,,COHA=,0.020,,,

,再生液比重,,γOHA=,1.021,g/cm3,,

,再生液體積,,VOH=,10.385,m3,,

,配酸稀釋用水量,,VOH1=,9.874,m3,,

,再生液流速,,WOH=,3.00,m/h,,

,進再生液時間,,tzA=,29.38,min,,

,置換時間,,tA3=,35.00,min,,

,置換流速,,WA3=,3.00,m/h,,

,置換用水量,,VA03=,12.37,m3,,

,小反洗流速,,WA01=,10.00,m/h,,

,小反洗時間,,tA1=,15.00,min,,

,小反洗用水量,,VA01=,17.67,m3/h,,

,小正洗時間,,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,,

,正洗時間,,tA5