孔道结构对柴油机微粒捕集器工作特性的影响

针对柴油机微粒捕集器中灰烬颗粒的沉积特征,设计了一种非对称孔道微粒捕集器,基于非对称孔道微粒捕集器对微粒捕集器再生模型进行修正,分析了非对称孔道对微粒捕集器再生特性的影响。研究结果表明,增大过滤体进出口截面比能减少微粒捕集器的压力损失,降低碳烟再生时过滤壁面的最大温度,且非对称孔道能减少灰烬沉积对再生时壁面最大温度的影响,因此根据过滤体壁面厚度适当增大进出口孔道截面比可以有效提升过滤体的碳烟承载量,延长微粒捕集器的车载使用寿命。     

柴油机微粒捕集器复合再生性能及其场协同分析

基于柴油机微粒捕集器瞬态复合再生机理,建立了CFD三维仿真模型,并利用漩涡破碎燃烧模型和场协同数学模型对柴油机微粒捕集器瞬态复合再生过程的速度矢量和温度梯度进行了数值模拟和场协同分析,结果表明,再生时间为175 s时的微粒捕集器过滤体后端壁面峰值温度达到1 184 K,且其过滤体内速度矢量和温度梯度的协同度最好,最优燃烧再生区域所占最大比值为0.58,表明此时微粒捕集器过滤体内再生燃烧速率最大,其再生效率最高。     

单纤维过滤介质表面尘粒捕集的随机模拟

基于控制面概念和粒子运动轨迹计算,建立单纤维过滤介质表面尘粒捕集的三维随机计算模型,采用Ku-wabara流场表征单纤维表面的气流绕流特征。计算分析了St数、无量纲粒径及单纤维过滤模型填充密度对沉积物形态结构和积尘状态下单纤维捕集效率的影响。结果指出,St数对沉积物形态结构具有显著作用,随St数减小,沉积物由紧密的堆积结构演变为分叉显著的树枝状结构。模拟结果还发现,无论过滤条件如何变化,无量纲单纤维捕集效率随捕集粒子数呈近似线性增加关系。     

催化型微粒捕集器的再生与压降数值研究

采用新的再生机理对催化型微粒捕集器（CPF）深床捕集微粒的氧化再生过程进行了建模，并将微粒捕集器中的压降分成5个部分分别计算，对其压降特性进行了数值研究。结果表明，新模型对深床捕集微粒的氧化再生计算与实验值吻合良好，比原模型更能反映微粒沉积的实际过程，深床捕集微粒的压降计算值也更精确。在排气流量大、温度高的工况下，深床捕集微粒的压降先迅速增大再减小的现象明显。研究结果能为工程应用提供验证手段，为CPF的优化设计提供依据。     

柴油车排气微粒捕集用复合金属丝网的制备与性能研究

论述了用于柴油车排气微粒捕集器的复合金属丝网的制备和测试过程，讨论了丝网层数和涂层负载对复合金属丝网过滤性能的影响，并分析了其捕集机理。     

柴油车排气微粒捕集用复合金属丝网的制备与性能研究

论述了用于柴油车排气微粒捕集器的复合金属丝网的制备和测试过程 ,讨论了丝网层数和涂层负载对复合金属丝网过滤性能的影响 ,并分析了其捕集机理     

燃油催化微粒捕集器在柴油机排气后处理中的应用研究

分析探讨了柴油机排气颗粒物的组成及危害,介绍了一种燃油催化微粒捕集器的结构及原理,结合发动机台架试验数据分析了该微粒捕集器对柴油机排气颗粒物的改善效果,同时研究了该微粒捕集器的强制再生过程以及对柴油机动力性和燃油经济性的影响.试验结果表明,该微粒捕集器具有较大的应用前景.     

柴油机微粒捕集器臭氧再生法离线再生

由R175型柴油机、微粒捕集器(Φ90 mm×150 mm)、CF-G10型臭氧发生器组成实验系统,进行了臭氧再生法离线再生研究。研究表明,在190℃温度下,再生气从DPF上游侧进气再生时,臭氧可以有效再生DPF,再生效率可达90%以上,再生效率达到65%左右时发生臭氧穿透,臭氧利用率下降;穿透时间点随微粒捕集时的柴油机载荷增大而提前,随微粒捕集时间增加而提前;臭氧供给量不变,再生气流量越大,再生效果越明显;再生气从DPF下游侧进气再生时,臭氧穿透时间点较上游侧进气再生滞后,但发生穿透后DPF几乎不再再生,总再生效率低于70%。结果表明,微粒捕集器臭氧再生法是可行的,对于如何提高臭氧利用率需进一步研究。     

颗粒层非稳态过滤捕集效率的研究

为计算颗粒层非稳态过滤效率，通过改进经典过滤理论模型，考虑颗粒在过滤介质中的沉积，理论推导得出非稳态过滤效率的计算公式，而经典颗粒层过滤效率计算公式仅为此计算公式的特例。因为理论计算公式是隐函数，不便于工程实际应用，所以，在常温条件下，对非稳态过滤时的过滤时间、过滤风速、过滤层厚度、粉尘浓度和颗粒层滤料均粒径等五个因素进行了正交实验研究。采用多元回归的方法得出各影响因素与过滤效率呈显性关系的效率关联计算公式，其计算结果与实验测试结果基本吻合。     

燃煤剂再生微粒捕集器在柴油机排气后处理中的应用研究

分析探讨了柴油机排气颗粒物的组成及危害,介绍了一种燃媒剂再生微粒捕集器（Fuel Borne Catalyst Diesel Particulate Filter,FBC-DPF）的结构及原理,并结合发动机台架试验数据,分析了该微粒捕集器对柴油机排气微粒的改善效果,同时研究了该微粒捕集器的强制再生过程,以及对柴油发动机的动力性和燃油经济性的影响。试验结果表明,该微粒捕集器具有较大的应用前景。     

湿法烟气脱硫系统中折板式除雾器性能的数值模拟

采用CFD软件对湿法烟气脱硫系统中广泛使用的折板式除雾器的主要性能进行了数值模拟。建立了数学模型，对气体相采用基于雷诺时均方程的SST ｋ-ω湍流模型封闭N-S方程，对液滴相采用基于Euler-Lagrange的DPM方法。通过调节除雾器的结构参数和工作参数，揭示了气液两相流动的流场，分析了结构参数对除雾器分离效率和工作压力降的影响，可用于湿法烟气脱硫系统中折板式除雾器的设计和优化。     

旋风除尘器流场及浓度场实验与模拟

在研究旋风除尘器内气固两相的运动状况及分离机理方面,计算机模拟替代部分实验的方法能够优化设计旋风除尘器结构参数,提高其对微细颗粒的捕集效率,减少运行压力损失。本研究采用RSM模型和随机轨道模型对旋风除尘器内流场及浓度场进行模拟及实验。研究表明,旋风除尘器压力损失模拟结果与实验结果吻合较好,对于大于5μm的颗粒其捕集效率模拟结果与实验结果基本吻合;旋风除尘器外壁的颗粒浓度呈螺旋带状分布;如将排气管管径减少至原直径0.8倍,可使其对2μm颗粒捕集效率提高6.6%,但压力损失提高36.5%;颗粒的凝并作用有利于提高旋风除尘器微细颗粒的捕集效率。     

固定床中粒状脱硫剂除尘效率的研究

建立了非稳态过滤下的固定床颗粒层除尘效率模型.该模型尽可能地包含了影响固定床颗粒层除尘的参数,反映了沉积粉尘对除尘效率的影响；研究了以粒状脱硫剂为滤料的固定床在不同颗粒层厚度、空床气速、粒径下的除尘效率.结果表明,在颗粒层厚度为400～800 cm、空床气速≤0.4 m/s的条件下,颗粒层的除尘效率可达90％以上.     

Feasibility of granular bed filtration of an aerosol of ultrafine metallic particles including a pressure drop regeneration system

A process for filtering an aerosol of ultrafine metallic particles (UFP) has been designed and tested, based on the principle of a multistage granular bed. The filtration system comprised a succession of granular beds of varying thickness composed of glass beads of different diameters. This system allows the pressure drop to be regenerated during filtration (“on-line” mode) using a vibrating probe. Tests monitoring the pressure drop were conducted on a “10-L/min” low airflow rate device and on a “100-m³/hr” prototype. Granular bed unclogging is automated on the latter. The cyclic operation and filtration performances are similar to that of filter medium-based industrial dust collectors.

Implications:?Filtration of ultrafine metallic particles generated by different industrial processes such as arc welding, metal cutting, or spraying constitutes a difficult problem due to the high filter clogging properties of these particles and to the high temperatures generally encountered. Granular beds represent an advantageous means of filtering these aerosols with difficult properties.     

滤袋数目对翼形上进风袋式除尘器内流场影响的数值模拟研究

针对实际运行过程中,袋式除尘器滤袋使用寿命短,压力损失过大的问题,本文以翼形上进风袋式除尘器为研究对象,采用CFD(computational fluid dynamics)技术模拟分析不同滤袋数(分别为92、88、84、80、76和72)时袋式除尘器内气流分布和压力损失规律。主要考察了流量分配系数、最大流量不均幅值、气流迹线、滤袋表面速度分布与压降等指标。结果表明,滤袋数为76个时,气流分布最为均匀,各滤袋负载均衡;相同过滤速度下,装置的压降随滤袋数目的增加而上升,即压降大小顺序为9288847672;与72个滤袋相比,76个滤袋的可用过滤面积更大。综合考虑,袋式除尘器的最优滤袋数目为76个。模拟结果为袋式除尘器的设计和优化提供了依据。     

Reducing pressure drop in a baghouse using flow distributors.

The pressure drop of ladder vanes in a baghouse could be reduced by decreasing the vane number and adjusting the inclined angle of the vane. Two types of flow distributors were utilized to test pressure drop caused by the structure of a baghouse. The pressure drops were measured by an inclined manometer under various filtration velocities. The purpose of this study is to understand the improvement effect of pressure drop saving for the traditional ladder vanes. Experimental results showed that the pressure drop of the Vane 3-1 configuration (flow distributor with three vanes perpendicular to the inlet flow) was higher than that of the Empty configuration (without flow distributors). The Vane 3-1 configuration could not reduce the pressure drop because of the barrier effect. By reducing the number and adjusting the angle of the vanes, the barrier effect was decreased, and the pressure drop of the Vane 2-1 configuration was much lower than that of the Vane 3-1 configuration. The largest difference in pressure drop between Vane 2-1 and Vane 3-1 was 1.702 cm w.g. at a filtration velocity of 4.17 cm/sec and, in terms of percentage, is 18.52% corresponding to a filtration velocity of 2.25 cm/sec. The improvement effect on the pressure drop saving for Vane 3-1 was significant.     

Reducing Pressure Drop in a Baghouse Using Flow Distributors

ABSTRACT

The pressure drop of ladder vanes in a baghouse could be reduced by decreasing the vane number and adjusting the inclined angle of the vane. Two types of flow distributors were utilized to test pressure drop caused by the structure of a baghouse. The pressure drops were measured by an inclined manometer under various filtration velocities. The purpose of this study is to understand the improvement effect of pressure drop saving for the traditional ladder vanes.

Experimental results showed that the pressure drop of the Vane 3-1 configuration (flow distributor with three vanes perpendicular to the inlet flow) was higher than that of the Empty configuration (without flow distributors). The Vane 3-1 configuration could not reduce the pressure drop because of the barrier effect. By reducing the number and adjusting the angle of the vanes, the barrier effect was decreased, and the pressure drop of the Vane 2-1 configuration was much lower than that of the Vane 3-1 configuration. The largest difference in pressure drop between Vane 2-1 and Vane 3-1 was 1.702 cm w.g. at a filtration velocity of 4.17 cm/sec and, in terms of percentage, is 18.52% corresponding to a filtration velocity of 2.25 cm/sec. The improvement effect on the pressure drop saving for Vane 3-1 was significant.     

新型颗粒层过滤性能的宏观数学模型

根据固定床颗粒层内气流含尘浓度的连续方程、颗粒层过滤规律和新型颗粒层的过滤特点，建立了固定床颗粒层过滤过程和新型颗粒层过滤性能的宏观数学模型；根据颗粒层的过滤机理和实际灰尘颗粒粒径的分布状态，在实验的基础上，修正了过滤速度对颗粒层过滤效率的影响；根据实验结果对过滤效率方程式、床层压降方程式中的特征参数进行了回归，得到了具体过滤介质的颗粒层宏观过滤数学模型。模型表明新型颗粒层过滤过程是一个不随过滤时间变化的准稳态过程，只与过滤介质特性和循环清灰周期有关，模型计算值能准确地反映颗粒层的过滤性能。     

Fine Particle Collection Efficiency Related to Pressure Drop,Scrubbant and Particle Properties,and Contact Mechanism

Collection efficiencies are shown for control of fine particles in venturi scrubbers (1) as a function of pressure drop, and (2) as a function of throat area and liquid to gas ratio. A relationship of pressure drop to throat area, gas density, throat velocity, and liquid to gas ratio is given and is used to provide a method for estimating efficiency knowing only these scrubber design parameters. The effect of charged particles and of surface active agents on collection efficiency are discussed briefly.     

Electrostatic Stimulation of Fabric Filtration

The concept of electrostatic stimulation of fabric filtration (ESFF) has been investigated at pilot scale. The pilot unit consisted of a conventional baghouse in parallel with an ESFF baghouse, allowing direct comparison. All results reported in this paper are for pulse-cleaned bags in which the electric field was maintained parallel to the fabric surface. The performance of the ESFF baghouse has been superior to the parallel conventional baghouse by several measures. The ESFF baghouse demonstrated: (1) a reduced rate of pressure drop increase during a filtration cycle, (2) lower residual pressure drop, (3) stable operation at higher face velocities, and (4) improved particle removal efficiency. These benefits can be obtained with only minor modifications to conventional pulse-jet hardware and at low electrical power consumption. The indicated ability to operate at increased face velocities with only modest expenditure for electrical hardware leads to very favorable economic projections.