單操實(shí)驗(yàn)-真空過濾-實(shí)驗(yàn)解說與數(shù)據(jù)處理課件

真空過濾

VacuumFiltration實(shí)驗(yàn)?zāi)康牧私庹婵者^濾之構(gòu)造及其批次操作方法。以布式漏斗做恒壓過濾實(shí)驗(yàn)，以決定實(shí)驗(yàn)式。研討濾餅之比阻與過濾介質(zhì)之阻力隨過濾壓力之變化。實(shí)驗(yàn)理論布式漏斗轉(zhuǎn)接頭真空壓力計(jì)真空抽氣機(jī)取2張12.5cm的濾紙置入布式漏斗中以10mL的水潤濕。實(shí)驗(yàn)步驟打開真空抽氣機(jī)，利用控制閥門調(diào)整至所欲之真空度(100mm-Hg)後，關(guān)閉真空室閥門。實(shí)驗(yàn)步驟

從濾液體積為25mL開始記錄(t1)，每收集25mL記錄其時(shí)間(t)，直到濾液體積至225mL為止。實(shí)驗(yàn)步驟225mL25mL清洗漏斗，倒出廢液後，增加真空度至200mm-Hg及400mm-Hg後重複上述步驟。不鎖緊真空室，即真空度為零的狀態(tài)下，重複上述步驟，記錄收集到濾液體積對(duì)時(shí)間之關(guān)係。增加泥漿之固含量至4%及6%，以真空度為200mm-Hg重複上述步驟。實(shí)驗(yàn)步驟實(shí)驗(yàn)數(shù)據(jù)Kaolinite(g)555.02510.0515.05H2O(mL)250.61250.43251.13250.54250.35252.13

NO.1NO.2NO.3NO.4NO.5NO.6固含量(%)2%2%2%2%4%6%壓力(Pa)013332.2426664.4753328.9513332.2413332.24濾液體積V(m3)收集時(shí)間t(sec)0.00002516.62.582.941.414.67.680.00005035.088.046.603.1410.7917.100.00007557.1510.808.945.4817.4228.340.00010077.0619.5512.797.2328.8941.710.000125102.2227.9516.189.4941.6559.640.000150125.4639.3520.0612.5456.3577.190.000175158.0447.2826.6415.6271.1893.350.000200205.3757.8033.4918.9798.15129.520.000225206.0771.1534.5724.32112.24158.4濾餅重量(g)18.3716.7216.3616.3125.4532.53烘乾後濾餅重量(g)4.777.567.027.6512.2416.73起始含水率Ci(%)989898989694最終含水率Cf(%)745557535249C0.02170.02090.02100.02090.04360.0680實(shí)驗(yàn)數(shù)據(jù)

NO.1NO.2NO.3趨勢線公式y(tǒng)=2.0000E+09x+627752y=1.0000E+09x+88659y=2.0000E+08x+110154R2值R2=0.877R2=0.9643R2=0.7517

NO.4NO.5NO.6趨勢線公式y(tǒng)=2.0000E+08x+50705y=2.0000E+09x+126246y=2.0000E+09x+237383R2值R2=0.9609R2

=0.9838R2=0.971實(shí)驗(yàn)數(shù)據(jù)圖實(shí)驗(yàn)數(shù)據(jù)濾器直徑(D)(m)0.135濾餅面積A(m2)0.014307濾液黏度(Pa*s)0.001布式漏斗直徑

NO.1NO.2NO.3NO.4NO.5NO.6斜率(S)(s/m6)2.0000E+091.0000E+092.0000E+082.0000E+082.0000E+092.0000E+09截距(I)(s/m3)6277528865911015450705126246237383實(shí)驗(yàn)數(shù)據(jù)

NO.1NO.2NO.3NO.4NO.5NO.6過濾比阻抗r(m-2)01.1423E+114.5791E+109.1204E+104.7631E+117.4224E+11濾材之起始阻抗Rm(m-1)01.6911E+104.2021E+103.8686E