纤维素助滤剂的预敷过滤性能

对高黏度物料加入纤维素助滤剂的预敷过滤性能进行了研究,说明不同的预敷条件对预敷层的过滤性能会有很大影响。通过改变预敷压力和浓度,对纤维素滤饼层的过滤比阻、可压缩性系数和孔隙率进行了研究。实验表明,纤维素预敷层的比阻随压力增加而增加,随浓度增加而减小;孔隙率随压力增加而减小,随浓度增加而增加;可压缩性系数随浓度增加而增加。纤维素助滤剂为中等可压缩性物料,孔隙率大。研究结果可为高黏度物料用纤维素预敷过滤的工程应用提供参考。     

聚结层排布对高压天然气净化用滤芯过滤性能影响的实验研究

本工作利用聚结滤芯过滤性能实验装置,通过改变滤芯内部的滤材排布,研究了聚结层为单一滤材以及由不同滤材排布组合的滤芯过滤性能,分析了聚结层排布方式对过滤效率、压降、饱和度及液体分布的影响。结果表明,由单一滤材组成的滤芯过滤效率随滤材孔径减小而增大,但孔径最小时由于压降较高,导致滤芯综合过滤性能反而最差。疏油在前、亲油在后的聚结层排布方式可提高滤芯过滤效率、减少液滴二次夹带,且以两层相同滤材交错排列的滤芯过滤效率比单层滤材交错排列明显更高,压降也相对较低,使得综合过滤性能显著提升。继续增加进气侧的疏油滤材层数可延缓压降增长、提高运行寿命,滤芯稳态品质因子达到最大值(0.30 kPa-1)。聚结层排布方式对滤芯过滤性能的影响主要通过改变液体分布形式而实现,且末层滤材的通道结构变化是导致不同聚结层排布方式的滤芯过滤性能出现差异的主要原因。     

折叠滤芯气液过滤性能测试及优化

采用聚结型滤芯气液过滤性能实验装置,研究了油雾加载率和表观过滤速度对折叠滤芯过滤性能的影响及涂覆粘合剂对折叠滤芯过滤性能的优化作用。结果表明,涂覆粘合剂后,滤材抗张力强度明显增大,滤材孔径减小。随油雾加载率增大,滤芯过滤层液体运移通道数增加,通道压降升高。初始压降随表观过滤速度增加而升高。粘合剂主要凝固在渗透性低的区域,压降变化较小。表观过滤速度增加抑制了二次夹带,折叠滤芯过滤效率升高,而由于粘合剂脱落,涂覆粘合剂的滤芯过滤效率下降。表观过滤速度为0.10 m/s时,随油雾加载率增大,聚结在滤材表面的粘合剂抑制夹带,滤芯过滤效率升高。     

天然气用聚结过滤元件性能的测定与分析

为了评价目前天然气净化用滤芯气液分离性能,利用聚结型滤芯气液过滤性能的检测装置研究了滤芯的放置方式、滤芯的有效厚度及填充密度等相关因素对气液过滤性能的影响。结果表明：在相同条件下,滤芯垂直于地面放置比水平位置放置时排液较顺畅,气液过滤效果较好,并且压降至少降低25%;不同材质滤芯,随着滤芯厚度在6~32mm范围内增加,滤芯稳态压降增加,过滤器出口液滴浓度减小,过滤性能提高;滤芯的填充密度增加,滤芯压降增大,过滤器出口液滴浓度减小。     

Fe_3Al金属滤芯特性及在U-gas煤气化装置中的应用

为了解决U-gas粉煤气化工艺飞灰过滤器装置中陶瓷滤芯的断裂问题,分析了陶瓷滤芯和金属滤芯的性能差异,在装置中安装了国产改进2050型Fe_3Al金属滤芯并投运试验,研究了投运后合成气及飞灰特性、滤芯的微观形貌、过滤效率、流量-压差曲线、滤饼渗透性等特性。结果表明,在与陶瓷滤芯相同过滤精度条件下,Fe_3Al金属滤芯具有孔隙率高、渗透性高、压溃强度大等优势。投运结果表明,Fe_3Al滤芯投运3个月以来无断裂故障,在相近工况条件下,Fe_3Al滤芯运行平衡压差相比陶瓷滤芯下降了50%,且水洗塔悬浮物固含量由1 000~2 000 mg/L下降至100~500 mg/L。     

两性聚丙烯酰胺的合成与助滤性能研究

通过自由基溶液聚合，以丙烯酰胺、丙烯酸钠及２－丙烯酸亚胺基－２－甲基丙烷三甲基氯化铵为单体合成了两性聚丙烯酰胺，与结构相似的阳离子，阴离子和非离子聚丙烯酰胺对比研究了助滤性能，同时研究了助滤剂用量，溶液ｐＨ值等因素对助滤效果的影响。     

硅藻土-木桨纤维为助滤剂强化过滤过程的研究(英文)

In this paper, a study to enhance the filtration for solid/liquid materials difficult to be filtered, such as highly viscous, highly compactible or gel like materials, is presented. Filter aids diatomaceous earth and wood pulp cellulose are used to enhance the filtration by improving filter cake structure and properties in the filtration of a biological health product and a highly viscous chemical fiber polymer melt product. The property of solid/liquid systems, filtration at different flow rates, specific cake resistance, cake wetness, filtration rate, filtrate turbidity for filter aid selection and evaluation, and operation optimization are investigated. The results are successfully applied to industrial process, and can be used as a reference for similar filtration applications.     

高效节能过滤技术与强化过滤过程的途径

叙述了国内外过滤与分离技术的发展和趋势。介绍了在节能型压榨过滤、陶瓷过滤、纳米过滤等3种节能型过滤技术的研究进展与结果;并针对难过滤物料及高精度过滤与分离的要求,分析了难过滤物料的特点,针对酶解液过滤的应用实例,提出了改善物料性质和强化过滤的有效途径,即添加助滤剂进行掺浆过滤,降低比阻,控制滤饼厚度,降低滤饼阻力的薄层滤饼过滤,这2种强化过滤技术的集成应用于某个难过滤物料分离的应用实例。     

Aerosol filtration performance of nanofibrous mats produced via electrically assisted industrial-scale solution blowing

Highly efficient polyamide 6 (PA6)-based nanofibrous air filter media was developed for particulate matter (PM) removal in the ambient atmosphere. The PA6 nanofibrous mats exhibited 85% PM0.3 capture performance at a cost of 164 Pa pressure drop when the multiple-nozzle solution blowing system was set to 8 m/h fabric winding speed. However, an increase in the winding speed at a constant feeding rate lowered the filtration efficiency to 62% due to the less amount of nanofibrous mats collected on the substrate. The application of electrical field at the same parameters allowed us to produce a filter media having FFP3-level filtration performance, which means 99% PM0.3 capture performance. This was attributed to a fine fiber diameter (116 nm), higher solidity value (0.149), and lower average pore size (2.28 μm). These results show that the electrically assisted solution blowing provides a feasible route for the production of high-quality nanofibrous filter media.     

阳离子聚丙烯酰胺对克雷伯杆菌絮凝效果的研究

采用有机絮凝剂阳离子型聚丙烯酰胺对克雷伯菌菌悬液进行絮凝处理。探讨了浓度、pH值、温度、助滤剂对絮凝剂絮凝及过滤性能的影响,并采用光学显微镜和扫描电子显微镜对菌悬液、絮凝剂和絮体3个方面进行了絮凝形态观察。结果表明,絮凝剂浓度为0.08 g/L,pH=7,温度为37℃时絮凝效果最佳。添加助滤剂Al2(SO4)3.18H2O、CaCl2.2H2O后过滤效果有明显的提高,且絮凝颗粒增大,沉降速度加快。     

动态微孔膜过滤特性研究

以旋叶膜滤机作为过滤设备对光合细菌发酵液为过滤物料进行了动态微孔膜过滤特性的研究。将膜技术与动态过滤技术相结合是膜分离技术的一个热点,集二者各自的优点,对其进行研究和开发,既有理论意义,又有实用价值。在实验中研究了操作条件如转速、压力、浓度对微孔膜过滤速率的影响。过滤速率的衰减基本可分为2个阶段,即速率下降阶段和稳态过滤阶段。     

高效空气过滤用PTFE膜材料的结构和性能

聚四氟乙烯(PTFE)膜高效空气过滤材料以其过滤效率高、初始阻力小和无硼释放等优点,在电子工业洁净室中得到了广泛的应用,然而目前尚缺乏PTFE膜与传统滤材结构及性能的系统对比研究。本文选取了两种商业应用的PTFE膜高效滤材,采用扫描电子显微镜、孔径分析仪、自动滤材测试仪等多种表征手段对材料的微观结构和过滤性能与超细玻璃纤维(简称玻纤)滤材进行了较为全面的对比研究,结果表明,PTFE膜本质上也是一种纤维类滤材,其纤维平均直径为60～85nm,远低于玻纤滤材的668.8nm;高效PTFE膜的过滤效率与玻纤滤材相当,且其初始阻力不及玻纤滤材的50%,但PTFE膜滤材的容尘性能不及玻纤滤材,更适合应用于有再生或预过滤装置的场所。     

高压工况对天然气滤芯性能影响的实验研究

为探究高压工况下天然气滤芯的过滤性能变化规律及影响因素,选取了四种规格的滤芯为研究对象,开展了现场实验和实验室性能测试。发现在现场运行410 d后,四种滤芯的压差平均增长约20%,在相同气固过滤实验条件下压差增长速率更大,而四种滤芯的过滤效率和品质因子的差异相对缩小。高压工况下过滤材料压缩了7%~31%,大量颗粒嵌入过滤材料或沉积在表面,各过滤层的透气度普遍下降,而抗拉强度均有所上升。结果表明,选用孔径分布均匀的纤维材料、过滤精度梯级设计的复合材料,对过滤层打褶以及采用导流式骨架,均有助于滤芯在高压运行工况下长周期稳定可靠运行。     

Filter life comparison of different levels of nanofiber coated cleanable-surface filter for gas turbine

High-efficiency air filtration is a basic requirement for the most cost-effective operation of high-efficiency gas turbines. The filtration system protects the gas turbine from damaging debris. In gas turbine/dust collector applications, higher efficiency filtration could be achieved with nanofibers, which provide higher equipment protection than traditional media. With a nanofiber performance filter layer, the dust accumulates on the surface of the filtration media rather than within the media and could be cleaned off easily with a back pulse resulting in long filter life and a low-operating pressure drop. In this study five type of gas tribune nanofiber coated corrugated cellulose/synthetic filter media were developed. Nanofiber coating was adjusted for five filtration efficiency level, 50 ≤ E < 60, 60 ≤ E < 70, 70 ≤ E < 85, 85 ≤ E < 95 and 95 ≤ E, pore size and filter-life of the developed media were evaluated. One of the developed nanofiber coated media was also compared with two other commercial nanofiber coated gas tribune filter media, a glass fiber type filter media and a commercial fine fiber gas tribune filter media. It was seen that, with decreasing penetration levels due to nanofiber coating level, initial 30 cycle durations of filter life evaluation could reach about 229.9 to 250.7 min. Highest final cycle duration of 188.7 min belonged to cellulose/synthetic blend corrugated filter media with penetration of 13.66%. Nanofiber based surface filter media was cleaned up better than fine fiber media and final 30 cycle sequences were significantly higher. Surface of the nanofiber coated media was smoother when compared to fine fiber media and during the initial and final cycle test dust could not penetrate inside and could not hang to this smooth surface. So, with back pulse cleaning cake releasing have performed easily. It was also seen that, for higher filter life nanofiber coating should be uniform and robust to back pulse cleaning.     

Maximizing the capacity and life of depth-type filters

An analytical expression has been derived for the variation of the filtration coefficient of depth-type filters with fractional depth from the downstream to the upstream face of the medium which satisfies the condition of identical retention in every cross-section of the medium. A numerical example has been worked out for a fibrous filter where the porosity of the medium was varied to comply with the required variation of the filtration coefficient. It has been shown also that a filter consisting of three uniform layers of different porosities may adequately approximate the required continuous variation of the filtration coefficient. After a retention of 10% pore volume of dust the permeability of the three-layer medium is about 4 times greater than that of a medium of uniform initial porosity characterized by identical initial collection efficiency, thickness and fiber diameter.     

粉尘在过滤布袋上沉积规律的研究

通过单因素实验研究了工艺操作参数如粉尘含量、平均过滤速度和单位过滤面积的加料量(简称面加料量)对粉尘在布袋上沉积规律的影响.研究结果表明,粉尘在布袋长度方向上分布不均,中间凸起,上下两端逐渐减薄;在平均过滤速度和面加料量一定时,粉尘含量对粉尘层分布的影响可以忽略不计;平均过滤速度和面加料量对粉尘层的影响显著.还采用Gu...     

液力过滤与液力压密脱水的理论(一)

将滤室固定不变的板框或箱式压滤机的操作过程分成滤饼过滤阶段和液力压密脱水阶段两个过程来研究。在滤饼过滤阶段 ,应用表面过滤机理 ,采用传统的鲁思过滤基本方程和平均过滤比阻的理论进行研究。在液力压密脱水阶段 ,应用达西定律建立了液力压密基本微分方程 ,根据研究得出滤饼渗透系数与孔隙率在压密脱水阶段的线性取代关系的结论 ;滤室固定的限制条件和物料平衡条件 ,推导出液力压密的脱水方程式。分析了影响液力压密脱水的时间因素和液力压密速率的各操作参数。建立了完整的液力过滤和压密脱水理论 ,为自动压滤机的设计提供了理论指导     

Measurements of Growth Rate of Filter Cake in Vertical Single-Pass Ultrafiltration Using Hollow Fiber Membrane Module

Vertical ultrafiltration experiments of silica colloid and bovine serum albumin solution were conducted in the single-pass mode by using a hollow fiber membrane module and beneficial in measuring the time evolution of the growth rate of the filter cake during filtration. The extremely small mass flux of the concentrate enabled us to highly concentrate the feed solution on the principle of vertical ultrafiltration in which the filter cake formed on the membrane surface is exfoliated continuously. Both growth and re-entrainment rates of the filter cake formed in vertical ultrafiltration were evaluated from the experimental data of the filtration rate and the mass fraction ratio of the concentrate on the basis of the mass balance within the hollow fiber membrane module. As a consequence, it was found that the re-entrainment rate of the filter cake increased almost linearly with the filtration time in the initial period of filtration and then tended to rapidly approach a constant value. The filter cake stopped growing under this dynamically balanced condition. The variations of the average specific resistance of the filter cake with time were also determined from the time evolutions of both the filtration rate and the growth rate of the filter cake.     

Experimental and analytical modeling of the filtration mechanisms of a paper stack candle filter

A candle filter consisting of a paper stack is an adequate device to clarify the grinding oil employed in the industrial post-processing of hard metal because of its cleaning efficiency and its regenerative capability by means of backwashing. The complex particle deposition mechanisms occurring in this device have not yet been investigated. Filtration experiments with a suitable particle-oil suspension were performed in a pilot filter and in a laboratory filter in order to investigate and model the mechanisms taking place in the process. The effect of operating parameters such as particle concentration and pressure difference on filter performance was evaluated. The results show that more than one filtration mechanism takes place simultaneously. While some depth filtration occurs at the beginning of the lifetime of a candle filter, blocking and cake filtration are the major mechanisms responsible for the filter clogging. Although blocking and cake filtration occur, to some extent, simultaneously, the cake filtration is the mechanism relevant for the modeling and scale-up of the long term filtration process.     

精密单丝滤布透水速率与截留精度的研究

为进一步了解液固分离用织造滤布的过滤性能,以液固分离用新型过滤介质精密单丝滤布为研究对象,对滤布结构、开孔大小、丝径、孔隙率等因素对透水速率的影响进行了理论分析与讨论;并采用国际标准规定的鼓泡孔径、透水速率和截留精度的测试方法,对几种精密单丝滤布的孔径大小、透水速率、截留精度、透水阻力、孔隙度、分离效率进行了实验测定;同时介绍了不同孔隙度及截留精度的测定方法和结果,并对截留精度经验计算进行了实验验证,对正确选择与科学使用过滤介质单丝滤布提供有益的参考。