过滤与分离
過濾與分離
과려여분리
FILTER & SEPARATOR
2015年
2期
20-23
,共4页
压滤机%滤布%铁矿%过滤%滤液
壓濾機%濾佈%鐵礦%過濾%濾液
압려궤%려포%철광%과려%려액
filter press%filter cloth%iron ore%filtration%filtrate
新增的四台metso隔膜压滤机投产后,发现随机进口的聚丙烯复丝滤布堵塞失效严重,不仅影响设备的效率,也增加了生产成本,为此选择三家国内滤布厂家在四台压滤机上进行了24个批次的滤布试验。结果表明:滤布有效循环数约1150,滤布单耗在30块/万吨精矿以上,滤饼水分远低于要求的9.3%,前300个循环和总体的滤液浓度分别为0.41%~0.97%和0.49%~0.73%,但滤布都未能满足1500的有效循环数和26块/万吨精矿单耗的要求。下一步拟减小尼龙丝径和滤布孔径,增大孔数和透气量,同时改善后续的表面处理工艺,可望解决滤液浓度和循环数量的矛盾。同时,对离散性很大的滤液浓度采用剔除可疑数据和数值积分求平均值的计算方法进行了科学的处理。
新增的四檯metso隔膜壓濾機投產後,髮現隨機進口的聚丙烯複絲濾佈堵塞失效嚴重,不僅影響設備的效率,也增加瞭生產成本,為此選擇三傢國內濾佈廠傢在四檯壓濾機上進行瞭24箇批次的濾佈試驗。結果錶明:濾佈有效循環數約1150,濾佈單耗在30塊/萬噸精礦以上,濾餅水分遠低于要求的9.3%,前300箇循環和總體的濾液濃度分彆為0.41%~0.97%和0.49%~0.73%,但濾佈都未能滿足1500的有效循環數和26塊/萬噸精礦單耗的要求。下一步擬減小尼龍絲徑和濾佈孔徑,增大孔數和透氣量,同時改善後續的錶麵處理工藝,可望解決濾液濃度和循環數量的矛盾。同時,對離散性很大的濾液濃度採用剔除可疑數據和數值積分求平均值的計算方法進行瞭科學的處理。
신증적사태metso격막압려궤투산후,발현수궤진구적취병희복사려포도새실효엄중,불부영향설비적효솔,야증가료생산성본,위차선택삼가국내려포엄가재사태압려궤상진행료24개비차적려포시험。결과표명:려포유효순배수약1150,려포단모재30괴/만둔정광이상,려병수분원저우요구적9.3%,전300개순배화총체적려액농도분별위0.41%~0.97%화0.49%~0.73%,단려포도미능만족1500적유효순배수화26괴/만둔정광단모적요구。하일보의감소니룡사경화려포공경,증대공수화투기량,동시개선후속적표면처리공예,가망해결려액농도화순배수량적모순。동시,대리산성흔대적려액농도채용척제가의수거화수치적분구평균치적계산방법진행료과학적처리。
With four sets of new Metso diaphragm filter press putting into production, the Polypropylene multifilament filter cloth imported with the equipment was found blocking seriously, which not only influenced the efficiency but increased the pro?duction cost. The domestic nylon monofilament filter cloths were selected from three factories and performance tests of 24 batches were conducted on four filter press. The test results showed that the effective cycle number of cloth was about 1150, filter cloth consumption was more than 30 pieces/million tons ore, moisture of filter cake was far below the requirement of 9.3%, the filtrate concentration of the first 300 cycles and the total was 0.41~0.97%and 0.49~0.73%, but it was failed to meet the effective circula?tion 1500 number and 26 pieces/million tons of concentrate. The further step should be to reduce the nylon wire diameter and fil?ter aperture, increase the number of holes and air permeability, as well as improve the surface treatment technology to solve the contradiction between the filtrate concentration and cycle number. At the same time, the concentration of filtrate with dubious da?ta was treated by the calculating methods of suspicious data rejection and the numerical integration for the mean value.