箱板紙造紙車間抄紙工段生產(chǎn)的漿水平衡計算案例目錄TOC\o"1-3"\h\u11572箱板紙造紙車間抄紙工段生產(chǎn)的漿水平衡計算案例 124826第一節(jié)工藝技術(shù)參數(shù) 120721第二節(jié)計算過程 23813第三節(jié)漿水平衡總表 19第一節(jié)工藝技術(shù)參數(shù)表3-1年產(chǎn)50萬噸高檔箱板紙漿水平衡生產(chǎn)參數(shù)序號指標名稱單位定額備注1定量g／m2275計算定量2設(shè)計車速m／min10153凈紙寬度mm43004紙機抄寬mm42405合格率%976抄造率%977成品率%958干損紙率%1.5對總絕干量H9成紙干度%9310進后干燥紙頁干度%7511進前干燥紙頁干度%4612面施膠量%1.0對絕干成品13底填料量%3.0對絕干成品14芯填料量%12.0對絕干成品15表面施膠量g／m28雙面計16表面施膠液濃度%1117噴淋淀粉量g／m21對成品計18噴淋淀粉溶液濃度%819進壓榨紙頁干度%2020壓榨白水帶出纖維率%0.15對其進漿量21壓榨濕損率%0.5對總絕干量22進真空伏輥紙頁干度%1223真空伏輥損紙率%1.0對其進漿量24真空伏輥帶出纖維率%0.18對總絕干量25沖邊寬度mm2×20切兩個紙邊26紙頁橫向收縮率%227底層后真空箱帶出纖維率%3對其進漿量28進底網(wǎng)后真空箱紙頁干度%629紙機補充清水量L8000噸成品計30面層：芯層：底層20：60：20以275g／m2計31底，芯層上網(wǎng)濃度%0.7532面層上網(wǎng)濃度%0.6533底，芯層壓力篩排渣率%6對其進漿量34底，芯壓力篩排渣濃度%235面層壓力篩排渣率%3對其進漿量36面層壓力篩排渣濃度%237日工作時間h/d22.538年工作日數(shù)d/y340第二節(jié)計算過程本設(shè)計的計算過程統(tǒng)一設(shè)定每噸成紙中水分含量為7%卷曲部（1）復(fù)卷部卷曲部Q2VQ成紙干度Q1V1C1C0=CQV0=1000.0000成品率干損池復(fù)卷、完成整理K1=95%干損池復(fù)卷、完成整理Q0VQQ0=V0C0=1000.0000×93%=930.0000 成品庫成品率K1=成品庫V2=V0/K1=1000.0000÷95%=1052.6316V1=V2?V0=1052.6316?1000.0000=52.6316Q2=V2×C2=1052.6316×93%=978.9474Q1=Q2?Q0=978.9474?930.0000=48.9474壓光、卷取部已知：Q2=978.9474 V2=1052.6316 復(fù)卷、完成整理后干燥部壓光、卷曲Q3V3C3干損池Q4V4C4Q2V2C2復(fù)卷、完成整理后干燥部壓光、卷曲Q干損池QQ抄造率K2=97%干損紙率d1=1.5%（對理論抄造量）計算： 抄造率K2=損紙損紙包含干損紙、濕損紙兩部分設(shè)X=抄造量+抄造損紙量則X=V2/K2=1052.6316÷97%=1085.1872設(shè)Y為X中絕干纖維量Y=Q2/K2=978.9474÷97%=1009.2241Q3=Y×d1=1009.2241×1.5%=15.1384V3=Q3/C3=15.1384÷93%=16.2778Q4=Q3+Q2=15.1384+978.9474=994.0858V4=V2+V3=1052.6316+16.2778=1068.9094表面施膠Q5V表面施膠QW2W蒸發(fā)水Q4=994.0858蒸發(fā)水后干燥V4=1068.9094后干燥Q4V4C4Q壓光卷曲部計算：壓光卷曲部Q5=Q4=994.0858V5=Q5/C5=994.0858÷76%=1308.0076Q6V6C6后干燥部Q7V7C7前干燥部施膠機W1Q后干燥部Q前干燥部施膠機（4）施膠部膠料已知：膠料Q5=994.0858Q5V5CQ表面施膠劑用量為：4g／m2面，計8g／m2成紙定量：275g／m2表面施膠劑的濃度為C6=11%Q6=（8/275）×930=27.0545V6=Q6/C6=27.0545÷11%=245.9500Q7=Q5?Q6=994.0858?27.0545=967.0313V7=V5?V6=1308.0076?245.9500=1062.0576壓榨部（5）前干燥部壓榨部Q8QQ7=967.0313W2V7W蒸發(fā)水前干燥C7=75%蒸發(fā)水前干燥施膠機Q7V7C施膠機Q計算：Q8=Q7=967.0313V8=Q8/C8=967.0313÷45%=2148.9584W2=V8?V7=2148.8584?1062.0576=1086.8008（6）壓榨部前干燥Q8V8C8前干燥Q真空伏輥壓榨部Q11V11C11QQ10V10CQ干損池Y=1009.2241干損池Q9V9C9一號稀白水Q一號稀白水池壓榨部白水帶出纖維率d2=0.15%（對進漿量）壓榨濕部損紙率d3=0.5%（對理論抄造量）計算：Q10=1009.2241×0.5%=5.0461設(shè)濕損紙平均干度為30%即C10=30%則V10=Q10/C10=5.0461÷30%=16.8203由：Q10=Y×d3=1009×0.5%=5.0450V10=Q10/C10=5.0450/30%=16.8167Q11=Q8+Q9+Q10=967.0313+0.15%Q11+5.0461Q11=973.5377Q9=Q11×d2=973.5577×0.15%=1.4603V11=Q11/C11=973.5377/20%=4867.6885V11+W=V8+V9+V10V9=（V11+W）－（V8+V10）=（4867.6885+8000）－（2148.9584－16.8167）=10701.9098C9=Q9/V9=1.4603/10701.9098=0.0136%真空伏輥已知：Q11=973.5377V11=4867.6885C11=20%假設(shè)：進真空伏輥紙頁的干度C14=12%進伏損池底損紙干度：C13=C11=20%真空伏輥帶出的纖維率d4=0.18%伏輥的濕損紙率d5=1.0%沖邊寬度：b=2×20mm橫向收縮率ε=2.0%紙機抄寬Bm=4240mm計算：底網(wǎng)后真空吸水箱濕紙頁寬度：底網(wǎng)后真空吸水箱Q14V14C14BeQQ13Q真空伏輥伏輥池r=b/（b+Be）=0.9161%真空伏輥伏輥池進入幅損池的濕紙量Q13是由Q9V9QQQ13=Y×d5+r×Q14一號稀白水池壓榨部Q12=Q14×d4一號稀白水池壓榨部Q14=Q11+Q12+Q13V14=Q14/C14V13=Q13/C13面芯底層復(fù)合輥V14=V11+V12+V13面芯底層復(fù)合輥代入數(shù)據(jù)得：Q16V16C16QQQ15V15C15Q一號稀白水池底網(wǎng)后真空吸水箱Q14=994.5310V14=8287.7583一號稀白水池底網(wǎng)后真空吸水箱Q14V14Q已知：Q14=994.5310V14=8287.7583C14=12%真空伏輥近底層后真空箱紙頁的干度C16=6%真空伏輥底層后真空箱帶出纖維率d6=3%計算：Q15=d6×Q16C15=Q15/V15Q16=Q14+Q15V16=V14+V15V16=Q16/C16代入已知條件得：Q15=30.7587V15=8800.4034C15=0.3495%Q16=1025.2897V16=17088.1617底層復(fù)合輥假設(shè)：已知：Q16=1025.2897V16=17088.1617C16=6%噴淋淀粉濃度：C18=6%噴淋淀粉加入量為1g／m2面芯復(fù)合紙層C17=C19=6%面芯復(fù)合紙層計算：以275g／m2為計算依據(jù)，Q19QQ18VQQ噴淋淀粉底層前真空吸水箱底層復(fù)合輥Q18=930/275=3.3800噴淋淀粉底層前真空吸水箱底層復(fù)合輥V18=Q18/C18Q16QQ17=20%（Q16－Q18）底層后真空吸水箱Q19=Q16－Q17－Q18底層后真空吸水箱V17=Q17/C17V19=Q19/C19代入已知條件得：Q17=193.7913V17=3229.8550Q19=828.1184V19=13801.9733底層前真空吸水箱底層成形板已知：Q17=193.7913V17=3229.8550C17=6%底層成形板Q21V21C21真空箱帶出纖維率：dQQ20V20CQ底層稀白水池底網(wǎng)前真空箱Q17=97%Q21底層稀白水池底網(wǎng)前真空箱V21=Q21/C21Q17V17C17VQ代入已知條件得：底網(wǎng)復(fù)合輥Q20=5.9935V20=2478.2821底網(wǎng)復(fù)合輥Q21=199.7848V21=5708.1371底層流漿箱底層成形板底層流漿箱已知：Q21=199.7848V21=5708.1371Q23V23QQ22Q底層濃白水池底層成形板漿料上網(wǎng)濃度C23=0.75%底層濃白水池底層成形板Q21V21C21計算：QQQ21=80%Q23V23=Q23/C23底層前真空吸水箱V22=V23－V21 底層前真空吸水箱代入已知條件得：Q22=49.9462V22=27589.3296C22=Q22/V22=0.1810%Q23=249.7310V23=33297.4667C23=Q23/V23=0.1810%底層流漿箱底層壓力篩已知：Q23=249.7310V23=33297.4667底層壓力篩Q25V25QQ24Q回流至沖漿泵口流漿箱上網(wǎng)濃度：C25=0.75%回流至沖漿泵口計算：Q24=10%Q25Q23V23C23QV25=Q25/C25底網(wǎng)成形板V25=V24+V23底網(wǎng)成形板代入已知條件得：Q24=27.7479V24=3699.7200Q25=277.4789V25=36997.1867底層壓力篩已知：Q25=277.4789V25=36997.1867底層沖漿泵C25=0.75%底層沖漿泵Q27V27QQ26V26CQ尾榨槽底層壓力篩Q25=94%Q27底層流漿箱尾榨槽底層壓力篩底層流漿箱V26=Q26/C26底網(wǎng)流漿箱Q25V25C25V底網(wǎng)流漿箱Q代入已知條件得：Q26=17.7114V26=885.5700Q27=295.1903V27=37882.7567底層成漿池C27=Q27/V27=0.7792%底層成漿池Q29VQ底層濃白水池Q28V28C28QQ24V24Q底層流漿箱回流底層沖漿泵C24=0.75%底層流漿箱回流底層沖漿泵Q27=295.1903V27=37882.7567Q27VQC28=C22=0.1810%C29=3%底層壓力篩計算：Q24+Q28+Q29=Q27底層壓力篩V24+V28+V29=V27V28=Q28/C28V29=Q29/C29代入已知條件得：Q28=48.3839V28=26731.4261Q29=217.4827V29=7249.4239填料制漿來底層漿底層成漿池、配漿池填料制漿來底層漿Q30V30C30Q31V31QQQ0=930.0000C29=3%底層配漿池總填料用量為15%（對絕干成品計）底層配漿池底層成漿池其中底層占20%，來漿濃度C31=4%底層成漿池計算：Q30=20%×15%Q0Q29V29C29V31QQ30+Q31=Q29底層沖漿泵V30+V31=V29底層沖漿泵代入已知條件得：Q30=27.9000V30=2509.8564Q31=189.5827V31=4739.5675底網(wǎng)成形板底層濃白水池底網(wǎng)成形板Q22V22C22已知：QQC22=C28=0.1810%Q28V28C28Q底層濃白水池底層沖漿泵計算：Q22=Q28+Q32底層濃白水池底層沖漿泵底層稀白水池Q32V32C32V22底層稀白水池QC32=C22=C28代入已知條件得：C32=0.1810%底網(wǎng)前真空箱Q32=1.3437底網(wǎng)前真空箱Q20V20CQ底層稀白水池Q32V32C32Q底層濃白水池底層稀白水池Q32=1.3437V32=736.8144底層濃白水池底層稀白水池Q33V33C33計算：Q33=QQV33=V20+V32稀白水池C33=Q33/V33稀白水池代入已知條件得：Q33=7.6648V33=4202.1263芯層真空箱C33=0.1824%芯層真空箱Q35VQ已知：Q19=817.5278V19=10219.0975Q34V34C34Q面層真空箱面芯層復(fù)合輥假設(shè)：C34=C35=C19=8%，面層真空箱面芯層復(fù)合輥Q19V19C19QQ（面和底層漿配比各占20%）底層復(fù)合輥芯層60%底層復(fù)合輥計算：Q34=Q17Q35=Q19－Q34代入已知條件得：Q34=204.3819V34=2554.7738Q35=613.1459V35=7664.3238芯層真空箱面層真空箱芯層真空箱Q37V37C37已知：QQC34=8%Q36V36Q面層稀白水池面層真空箱面層真空箱來漿濃度：C37=4%面層稀白水池面層真空箱計算：Q36=d8×Q37Q34V34C34QQ面芯層復(fù)合輥V37=Q37/C37面芯層復(fù)合輥V36=V37－V34代入已知條件得：Q36=6.3211V36=2712.8012面層流漿箱Q37=210.7030V37=5267.5750面層流漿箱C36=0.2330%Q39VQQ38V38C38Q面層濃白水池面層成形板C37=4%面層濃白水池面層成形板Q37V37Q漿料上網(wǎng)濃度C39=0.65%面層真空箱計算：Q38=30%Q39面層真空箱Q37=70%Q39V39=Q39/C39V38=V39－V37代入已知條件得：Q38=90.3013V38=41040.7789C38=0.2200%Q39=301.0043V39=46308.3539面層壓力篩面層流漿箱面層壓力篩Q41V41C41已知：QQQ40V40Q流漿箱回流率為10%回流至沖漿泵口面層流漿箱流漿箱上網(wǎng)濃度C41=0.65%回流至沖漿泵口面層流漿箱Q39V39C39QQ39=90%Q41面網(wǎng)成形板V41=Q41/C41面網(wǎng)成形板V41=V39+V40一段除渣器代入已知條件得：一段除渣器Q40=33.4450V40=5145.3692Q43V43C43QQQ42Q尾渣槽面層壓力篩已知：Q41=334.4492V41=51453.7231尾渣槽面層壓力篩C41=0.65%Q41Q面層流漿箱排渣濃度：1.4%面層流漿箱計算：Q42=3%Q43Q41=97%Q43V42=Q42/C42V43=V41+V42代入已知條件得：Q42=10.3438V42=738.8429Q43=344.7930V43=52192.5660C43=0.6606%一段除渣器已知：Q43=344.7930V43=52192.5660假設(shè)：一段除渣器排渣率23%，進漿濃度為0.83%Q44V44C44Q45QQ面層沖漿泵去二段除渣器一段除渣器Q43=77%Q45去二段除渣器一段除渣器Q43V43C43V45QV44=V45－V43網(wǎng)面壓力篩代入已知條件得：網(wǎng)面壓力篩Q44=102.9901V44=1757.2051Q45=447.7831V45=53949.7711面層沖漿泵及三層除沙系統(tǒng)面層成漿池面層沖漿泵回流來面層成漿池面層沖漿泵回流來Q47V47C47QQQ面層沖漿泵面層沖漿泵Q45V45QQQ44QQ48V48CQ二段除渣器一段除渣器二段除渣器一段除渣器Q49V49CQQQQ50VQQ網(wǎng)面壓力篩QQQ56Q三段除渣器Q52Q一號稀白水池來一號稀白水池來排渣面層濃白池來排渣面層濃白池來已知：Q40=33.4450V40=5145.3692Q44=102.9901V44=1757.2051Q45=447.7831V45=53949.7711假設(shè)：三段除渣器的總排渣比率大約為2.2%（相對于一段除渣器的進口輸出漿量）進漿濃度：C50=0.83%，排渣濃度：C52=1.4%三段除渣器的排渣比率為18%（三段除渣器的進口出料量）二段除渣器進漿濃度：C48=0.83%排渣濃度：C49=1.4%稀白水池來白水濃度：C53=C54=C55=C73=0.2288%面層來濃白水濃度：C56=C38=0.2545%面層成漿池來漿濃度：C46=3%計算：Q52=2.2%Q45V52=Q52/C52Q52=18%Q50Q51=82%Q50V50=Q50/C50V51=V50－V52Q49+Q54=Q50V49+V54=V50V49=Q49/C49V54=Q54/C54Q44+Q51+Q53=Q48V44+V51+V53=V48V48=Q48/C48V53=Q53/C53Q48=Q47+Q49V48=V47+V49Q40+Q46+Q47+Q56=Q45V40+V46+V47+V56=V45V46=Q46/C46V56=Q56/C56Q55=Q53+Q54V55=V53+V54代入已知條件得：Q46=223.0258V46=7434.1934Q47=132.5995V47=18300.3159Q48=179.9860V48=21685.0661Q49=47.3865V49=3384.7502Q50=54.7289V50=6593.8434Q51=44.8777V51=5890.1863Q52=9.8512V52=703.6571Q53=32.1182V53=14037.6747Q54=7.3424V54=3209.0932Q55=39.4606V55=17246.7679Q56=58.7129V56=23069.8926面層成漿池制漿來面層漿膠料已知：Q46=223.0258V46=7434.1934制漿來面層漿膠料Q58V58C58Q57VQQ假設(shè)：面層膠料用量為0.9%（對絕干成品計）面層來漿濃度C58=4%面層配漿池計算：Q57=0.9%×20%Q0面層配漿池面層成漿池V58=Q58/C58面層成漿池Q46V46C46Q57QV57+V58=V46面層沖漿泵代入已知條件得：面層沖漿泵Q57=1.6740V57=1900.3984Q58=221.3518V58=5533.7950面網(wǎng)成形板面層濃白水池面網(wǎng)成形板Q38V38C38已知：QQQ56V56C56Q面層沖漿泵面層濃白水池Q38=90.3013V38=41040.7789面層沖漿泵面層濃白水池Q59V59C59計算：Q38=QQV38=V56+V59面層稀白水池C56=C38=C59面層稀白水池代入已知條件得：Q59=31.5884V59=17970.8863C59=0.2545%面層稀水池Q36V36C36面網(wǎng)前真空箱已知：QQ面網(wǎng)前真空箱Q59V59C59Q面層濃白水池面層稀白水池計算：Q60=Q36+Q59面層濃白水池面層稀白水池Q60V60C60V60QC60=Q60/V60代入已知條件得：一號稀白水池Q60=37.9095一號稀白水池V60=20683.6875C60=0.1833%芯層真空箱已知：Q35=613.1459V35=7664.3238芯層成形板C35=8%芯層成形板Q62V62CQQ61V61Q芯層真空箱計算：Q61=d9×Q62芯層真空箱芯層稀白水池Q35=（1－d9）×Q62芯層稀白水池Q35V35C35V62QV61=V62－V35面芯層復(fù)合輥代入已知條件得：面芯層復(fù)合輥Q61=16.3673V61=10850.7703Q62=629.5132V62=18515.0941芯層成形板芯層流漿箱已知：Q62=629.5132V62=18515.0941芯層流漿箱Q64V64CQQ63Q芯層濃白水池芯層成形板漿料上網(wǎng)濃度C64=0.71%芯層濃白水池芯層成形板Q62V62C62計算：QQQ62=79%Q64芯層真空箱V64=Q64/C64芯層真空箱V63=V64－V62代入已知條件得：Q63=167.3389V63=93717.5960Q64=796.8521V64=112232.6901C63=0.1786%芯層流漿箱已知：Q64=796.8521V64=112232.6901芯層壓力篩C64=0.71%芯層壓力篩假設(shè)：流漿箱回流率為9%Q66V66CQQ65V65CQ回流至沖漿泵入口芯層流漿箱Q64=91%Q66回流至沖漿泵入口芯層流漿箱V66=Q66/C66Q64V64C64VQ代入已知條件得：芯層成形板Q65=78.8095V65=11099.9296芯層成形板Q66=875.6616V66=123332.6197芯層沖漿泵芯層壓力篩芯層沖漿泵Q68V68C68已知：QQQ67V67Q壓力篩排渣率6%，排渣濃度：C67=2%尾渣槽芯層壓力篩計算：Q67=6%Q68尾渣槽芯層壓力篩Q66V66C66QV67=Q67/C67芯網(wǎng)流漿箱V68=V66+V67芯網(wǎng)流漿箱代入已知條件得：Q67=55.8933V67=2794.6650Q68=931.5549V68=126127.2847芯層濃白水池芯層成漿池泵芯層沖漿泵芯層濃白水池芯層成漿池泵Q69V69C69Q70VQQQ65V65QQ68=931.5549V68=126127.2847芯層流漿箱回流芯層沖漿泵C69=C63=0.1786%芯層流漿箱回流芯層沖漿泵Q68V68CQ計算：Q65+Q69+Q70=Q68V65+V69+V70=V68芯層壓力篩V69=Q69/C69芯層壓力篩V70=Q70/C70代入已知條件得：Q69=165.8657V69=92869.9468Q70=689.6697V70=22247.4083芯層成形板芯層濃白水池芯層成形板Q63V63C63已知：QQC69=C63=0.1786%Q69V69C69Q芯層沖漿泵芯層濃白水池計算：Q63=Q69+Q71芯層沖漿泵芯層濃白水池Q71V71C71V63=VQC63=C69=C71代入已知條件得：芯層稀白水池Q71=1.4732芯層稀白水池V71=847.6492C71=0.1786%Q61V61Q芯網(wǎng)前真空箱Q71V71C71Q芯層濃白水池Q71=1.4732V71=847.6492芯層濃白水池芯層稀白水池C71=0.1786%芯層稀白水池Q72V72C72計算：Q72QV72=V61+V71稀白水池C72=Q72/V72稀白水池代入已知條件得：Q72=17.8405V72=11698.4195C72=0.1525%底層后真空箱來壓榨部來真空伏輥來底面稀白水池芯網(wǎng)稀白水池面網(wǎng)稀白水池一號稀白水池底層后真空箱來壓榨部來真空伏輥來底面稀白水池芯網(wǎng)稀白水池面網(wǎng)稀白水池Q15V15C15Q9V9C9QQQQQQ一號稀白水池（Q一號稀白水池（Q73/V73/C73）Q83V83C83QQQQQQ多余白水去白水塔去面層除渣系統(tǒng)去伏輥損紙水力碎漿機多余白水去白水塔去面層除渣系統(tǒng)去伏輥損紙水力碎漿機已知：Q9=1.4603V9=10701.9098Q12=1.7902V12=3294.0543Q15=30.7587V15=8800.4034Q33=7.6648V33=4202.1263Q60=37.9095V60=20683.6875Q72=17.8405V72=11698.4195Q55=39.4606V55=17246.7679Q74=6.5790V74=2875.4560Q76=2.2700V76=992.0840計算：Q73=Q9+Q12+Q15+Q33+Q60+Q72V73=V9+V12+V15+V33+V60+V72C73=Q73/V73Q55+Q74+Q76+Q83=Q73V55+V74+V76+V83=V73代入已知條件得：Q73=97.4240V73=59380.6008C73=0.1641%Q83=49.1144V83=38266.2929C83=0.1283%一號稀白水池來水力碎漿機一號稀白水池來Q74V74C74已知：QQQ3V3C3Q1VQQ假設(shè)：C74=C73=0.2288%C75=2.4%壓光卷曲部復(fù)卷部水力碎漿機計算：Q1+Q3+Q74=Q75壓光卷曲部復(fù)卷部水力碎漿機Q75V75C75V1+V3Q代入已知條件得：Q74=6.5790V74=2875.4560損紙漿塔Q75=70.6648V75=2944.3652損紙漿塔一號稀白水池來伏損池一號稀白水池來Q76V76C76已知：Q10=QQ13=19.2031V13=96.0155Q10V10C10Q13VQQ壓榨部真空伏輥伏損池計算：Q10+Q13+Q76=Q77壓榨部真空伏輥伏損池V10+V13+V76=V77Q77QQ76=2.2700V76=992.0840損紙漿塔Q77=26.5180V77=1104.9162損紙漿塔損紙漿塔和圓網(wǎng)濃縮機已知：Q75=70.6648V75=2944.3652Q77=26.5180V77=1104.9162假設(shè)：圓網(wǎng)濃縮機帶出纖維率：d10=0.9%濃縮后漿的濃度為：C80=2.9%計算：Q75+Q77=Q78伏損池來水力碎漿機來Q77V77C77Q75V75伏損池來水力碎漿機來QQ損紙漿塔Q79=0.9%Q78損紙漿塔Q78V78C78QQ79V79C79VQV78=V79+V80二號稀白水池圓網(wǎng)濃縮機代入已知條件得：二號稀白水池圓網(wǎng)濃縮機Q80V80C80QQQ79=0.8746V79=728.3090C79=0.1201%Q80=96.3082V80=3320.9724打漿前損紙池打漿前損紙池芯層配漿池已知：Q80=96.3082V80=3320.9724Q82V82C82制漿來芯層漿QQ制漿來芯層漿Q80VQQ填料打漿后損紙池芯層配漿池其中芯層占80%，來漿濃度C82=4%填料打漿后損紙池芯層配漿池計算：Q81=80%×15%Q0芯層成漿池Q80+Q81+Q82=Q70芯層成漿池Q70V70C70V80+V81QV82=Q82/C82芯層沖漿泵代入已知條件得：芯層沖漿泵Q81=111.6000V81=6882.3984二號稀白水池來一號稀白水池來Q82=481.7615V82=12044.0375二號稀白水池來一號稀白水池來Q79V79CQQ已知：Q79=0.8746V79=728.3090Q83=49.1144V83=38266.2929白水塔計算：Q84=Q79+Q83白水塔V84=V79+V83Q84V84C84VQ代入已知條件得：去制漿車間回用Q84=49.9890V84=38994.6019去制漿車間回用C84=0.1282%第三節(jié)漿水平衡總表表3-2漿水平衡明細表序號單元名稱來源于去向纖維漿料收支收支1復(fù)卷、完成整理部來自卷曲部978.94741052.6316去成品庫930.00001000.0000去干損池48.947452.6316合計978.9474978.94741052.63161052.63162壓光卷曲部來自后干燥994.08581068.9094去干損池15.138416.2778去復(fù)卷部978.94741052.6316合計994.0858994.08581068.90941068.90943后干燥來自表面施膠994.08581308.0076去壓光卷取部994.08581068.9094蒸發(fā)水239.0982合計994.0858994.08581308.00761308.00764施膠機來自前干燥967.03131062.0576去后干燥994.08581308.0076表面施膠劑27.0545245.9500合計994.0858994.08581308.00761308.00765前干燥來壓榨部967.03132148.9584去施膠機967.03131148.0076蒸發(fā)水1086.8008合計967.0313967.03132148.95842234.80846壓榨部來自真空伏輥973.53774867.6885去前干燥967.03132148.9584去干損池5.045016.8167去一號稀白水池1.460310701.9098清水8000.0000合計973.5377973.536612867.688512867.6849序號單元名稱來源于去向纖維漿料收支收支7真空伏輥來底網(wǎng)真空吸水箱994.53108287.7583去伏輥池19.203196.0155去一號稀白水池1.76023294.0543去壓榨部973.53774867.6885合計994.5310994.50108287.75838257.75838底網(wǎng)后真空吸水箱來面芯底層復(fù)合輥1025.289717088.1617去一號稀白水池30.75878800.4034去真空伏輥994.53108287.7583合計1025.28971025.289717088.161717088.16179底層復(fù)合輥來自面芯復(fù)合紙層828.118413801.9733噴淋淀粉3.380056.3333來底層前真空吸水箱193.79133229.8550去底層后真空吸水箱1025.289717088.1617合計1025.28971025.289717088.161617088.161710底層前真空吸水箱來自底層成形板199.78485708.1371去底層稀白水池5.99352478.2821去底層復(fù)合輥193.79133229.9733合計199.7848199.78485708.13715078.255411底層成形板來自底層流漿箱249.731033297.4667去底層濃白水池49.946227589.3296去底層前真空吸水箱199.78485708.1371合計249.7310249.731033297.466733297.4667序號單元名稱來源于去向纖維漿料收支收支12底層流漿箱來自底層壓力篩277.478936997.1867去回流至沖漿泵入口27.74793699.7200去底網(wǎng)成形板249.731033297.4667合計277.4789277.478936997.186736997.186713底層壓力篩來自底層沖漿泵295.190337882.7567去尾渣槽17.7114885.5700去底網(wǎng)流漿箱277.478936997.1867合計295.1903295.190337882.756737882.756714底層沖漿泵來自底層成漿池217.48277249.4239來自底層濃白水池48.482726731.4261去底層壓力篩295.190337882.7567來自底層流漿箱回流29.26433901.9067合計295.2297295.190337882.756737882.756715底層成漿池、配漿池來自制漿車間底層漿189.58274739.5675去底層沖漿泵217.48277249.4239來填料27.90002509.8564合計217.4827217.48277249.42397249.423916底層濃白水池來自底網(wǎng)成形板52.675829097.0876去底層沖漿泵51.332128360.2732去底層稀白水池1.3437736.8144合計52.675852.675829097.087629097.0876序號單元名稱來源于去向纖維漿料收支收支17底層稀白水池來自底網(wǎng)前真空箱6.32113465.3119來自底層濃白水池1.3437736.8144去稀白水池7.66484202.1263合計7.66487.66484202.12634202.126318面芯層復(fù)合輥來自芯層真空箱613.14597664.3238來自面層真空箱204.38192554.7738去底層復(fù)合輥817.527810219.0975合計817.5278817.527810219.097610219.097519面層真空箱來自芯層真空箱210.70305267.5750去面層稀白水池6.32112712.8012去面芯層復(fù)合輥204.38192554.7738合計210.7030210.70305267.57505267.575020面層成形板來自面層流漿箱301.004346308.3539去面層稀白水池90.301341040.7789去面層真空箱210.70305267.5750合計301.0043301.004346308.353946308.353921面層流漿箱來自面層壓力篩334.449251453.7231去回流至沖漿泵口33.44505145.3692去面網(wǎng)成形板301.004346208.3539合計334.4492334.449351453.723151453.723122面層壓力篩來自一段除渣器344.793051970.9131去尾渣槽10.3438517.1900去面層流漿箱334.449251453.7231合計344.7930344.793051970.913151970.9131序號單元名稱來源于去向纖維漿料收支收支23一段除渣器來自面層沖漿泵447.783153949.7711去二段除渣器102.99011978.8580去網(wǎng)面壓力篩344.793051970.9131合計447.7831447.783153949.771153949.771124面層沖漿泵及三段除渣系統(tǒng)來自面層成漿池223.02587434.1934來自面層沖漿泵33.44505145.3692來自面層濃白水池58.712923069.8926來自一號稀白水池39.460617246.7679去網(wǎng)面壓力篩344.793052192.5660排渣9.8512703.6571合計354.6443354.644252896.224052896.223125面層成漿池，配漿池來制漿系統(tǒng)面層漿221.35185533.7950來膠料1.67401900.3984去面層沖漿泵223.02587434.1934合計223.0258223.02587434.19347434.193426面層濃白水池來自面層成形板90.301341040.7789去面層沖漿泵58.712923069.8926去面層稀白水池31.588417970.8863合計90.301390.301341040.778941040.778927面層稀白水池來自面網(wǎng)前真空箱6.32112712.8012來自面層濃白水池31.588417970.8863去一號稀白水池37.909520683.6875合計37.909537.909520683.687520683.687528芯層真空箱來自芯層成形板