Saleem Mahmood, Khan Rafi Ullah, Tahir M Suleman, Krammer Gernot
Institut of Chemical Engineering and Technology, University of the Punjab, Quaid-i-Azam Campus, 54590-Lahore, Pakistan ; Graz University of Technology, Graz, Austria.
Institut of Chemical Engineering and Technology, University of the Punjab, Quaid-i-Azam Campus, 54590-Lahore, Pakistan.
Powder Technol. 2011 Dec 25;214(3-3):388-399. doi: 10.1016/j.powtec.2011.08.037.
Pulse-jet bag filters are frequently employed for particle removal from off gases. Separated solids form a layer on the permeable filter media called filter cake. The cake is responsible for increasing pressure drop. Therefore, the cake has to be detached at a predefined upper pressure drop limit or at predefined time intervals. Thus the process is intrinsically semi-continuous. The cake formation and cake detachment are interdependent and may influence the performance of the filter. Therefore, understanding formation and detachment of filter cake is important. In this regard, the filter media is the key component in the system. Needle felts are the most commonly used media in bag filters. Cake formation studies with heat treated and membrane coated needle felts in pilot scale pulse jet bag filter were carried out. The data is processed according to the procedures that were published already [Powder Technology, Volume 173, Issue 2, 19 April 2007, Pages 93-106]. Pressure drop evolution, cake height distribution evolution, cake patches area distribution and their characterization using fractal analysis on different needle felts are presented here. It is observed that concavity of pressure drop curve for membrane coated needle felt is principally caused by presence of inhomogeneous cake area load whereas it is inherent for heat treated media. Presence of residual cake enhances the concavity of pressure drop at the start of filtration cycle. Patchy cleaning is observed only when jet pulse pressure is too low and unable to provide the necessary force to detach the cake. The border line is very sharp. Based on experiments with limestone dust and three types of needle felts, for the jet pulse pressure above 4 bar and filtration velocity below 50 mm/s, cake is detached completely except a thin residual layer (100-200 μm). Uniformity and smoothness of residual cake depends on the surface characteristics of the filter media. Cake height distribution of residual cake and newly formed cake during filtration prevails. The patch size analysis and fractal analysis reveal that residual cake grow in size (latterly) following regeneration initially on the base with edges smearing out, however, the cake heights are not leveled off. Fractal dimension of cake patches boundary falls in the range of 1-1.4 and depends on vertical position as well as time of filtration. Cake height measurements with Polyimide (PI) needle felts were hampered on account of its photosensitive nature.
脉冲喷吹袋式过滤器常用于去除废气中的颗粒。分离出的固体在可渗透的过滤介质上形成一层,称为滤饼。滤饼会导致压力降增加。因此,必须在预定义的上限压力降或预定义的时间间隔处分离滤饼。因此,该过程本质上是半连续的。滤饼的形成和分离是相互依存的,可能会影响过滤器的性能。因此,了解滤饼的形成和分离很重要。在这方面,过滤介质是系统中的关键部件。针刺毡是袋式过滤器中最常用的介质。在中试规模的脉冲喷吹袋式过滤器中,对经过热处理和膜涂覆的针刺毡进行了滤饼形成研究。数据按照已发表的程序进行处理[《粉末技术》,第173卷,第2期,2007年4月19日,第93 - 106页]。这里展示了不同针刺毡上的压力降演变、滤饼高度分布演变、滤饼斑块面积分布以及使用分形分析对它们的表征。观察到,膜涂覆针刺毡的压力降曲线的凹度主要是由不均匀的滤饼区域负荷导致的,而对于热处理介质来说这是固有的。残留滤饼的存在会增强过滤循环开始时压力降的凹度。仅当喷射脉冲压力过低且无法提供分离滤饼所需的力时,才会观察到局部清洁。边界线非常清晰。基于对石灰石粉尘和三种针刺毡的实验,对于高于4巴的喷射脉冲压力和低于50毫米/秒的过滤速度,除了一层薄的残留层(100 - 200微米)外,滤饼会被完全分离。残留滤饼的均匀性和平滑度取决于过滤介质的表面特性。过滤过程中残留滤饼和新形成滤饼的滤饼高度分布占主导。斑块尺寸分析和分形分析表明,残留滤饼最初在底部再生,边缘逐渐模糊,随后尺寸增大(后期),然而,滤饼高度并未趋于平整。滤饼斑块边界的分形维数在1 - 1.4范围内,并且取决于垂直位置以及过滤时间。由于聚酰亚胺(PI)针刺毡的光敏性质,对其进行滤饼高度测量受到了阻碍。