本文關(guān)鍵詞：電袋除塵器結(jié)構(gòu)優(yōu)化的數(shù)值模擬研究　出處：《江西理工大學(xué)》2015年碩士論文　論文類型：學(xué)位論文

  更多相關(guān)文章： 電袋除塵器 捕集粒徑 開孔范圍 濾袋分布 數(shù)值模擬

【摘要】：當(dāng)今,粉塵對(duì)人體的危害和造成的自然環(huán)境污染越來(lái)越嚴(yán)重,且粉塵危害在事故總數(shù)中所占比例均較高,因此,人們對(duì)PM2.5的要求也越來(lái)越嚴(yán)格,研發(fā)高性能的除塵器有著重要意義。本文依據(jù)電袋除塵器結(jié)構(gòu)優(yōu)化的實(shí)際情況,通過(guò)經(jīng)典流體力學(xué)軟件FLUENT6.0以流體力學(xué)為基礎(chǔ)建立守恒方程組,分別采用uds電場(chǎng)編程與k-ε模型對(duì)電袋除塵器電場(chǎng)的建立與湍流現(xiàn)象進(jìn)行描述,進(jìn)行了電袋除塵器靜電區(qū)內(nèi)氣流分布、荷電顆粒運(yùn)動(dòng)軌跡、極板開孔導(dǎo)致的壓降變化及袋式區(qū)濾袋的分布的數(shù)值模擬研究。在數(shù)值模擬可信的基礎(chǔ)上,研究了不同因素(電場(chǎng)分布、極板開孔、濾袋分布等)對(duì)電袋除塵器結(jié)構(gòu)優(yōu)化的影響,得出最小去除粒徑、集塵板幾何因素、濾袋最佳分布方式,并結(jié)合流場(chǎng)參數(shù)變化情況對(duì)壓力變化機(jī)理進(jìn)行了分析。得出以下結(jié)論:(1)氣流方向的電場(chǎng)強(qiáng)度小于集塵板方向的電場(chǎng)強(qiáng)度,以放電線中心為最強(qiáng)。(2)當(dāng)放電線荷上45k V時(shí),靜電區(qū)產(chǎn)生穩(wěn)態(tài)電場(chǎng),電場(chǎng)會(huì)影響流場(chǎng)的分布。(3)靜電區(qū)最小捕集粒徑為1.5μm,得出對(duì)于電袋復(fù)合除塵器,在確定電壓下,可確定靜電區(qū)內(nèi)的最小捕集粒徑,隨著粒徑的增大受到電場(chǎng)力的作用越大粒子越容易被捕集;(4)集塵板適合開孔的范圍為0.324m至1.25m,在研究得出除塵器最小去除粒徑的條件下,可確定集塵板的開孔范圍。(5)通過(guò)分析該除塵器集塵板最佳開孔率為0.535,除塵器集塵板不會(huì)隨著開孔率增大除塵性能就越好,集塵板存在最佳開孔率;(6)通過(guò)分析該除塵器集塵板最佳孔徑大小為0.095,且隨著集塵板粗糙度增大,極板的磨損也增大;得出集塵板最佳開孔率及孔徑大小和集塵板磨損情況,有利于除塵器結(jié)構(gòu)設(shè)計(jì)及優(yōu)化的研究,結(jié)構(gòu)設(shè)計(jì)與實(shí)際相符合。為了提高集塵板使用壽命,在集塵板粗糙度的選擇需要慎重考慮。(7)濾袋的合理分布會(huì)影響濾袋的除塵效率。本文通過(guò)對(duì)電袋除塵器中的電場(chǎng)、流場(chǎng)、荷電顆粒、集塵板幾何因素、濾袋分布等因素進(jìn)行了模擬研究,為電袋除塵器結(jié)構(gòu)優(yōu)化提供一種參考方法。
[Abstract]:Nowadays, the harm of dust to the human body and the pollution caused by natural environment are more and more serious. The proportion of dust hazards in the total number of accidents is relatively high. Therefore, people's requirements for PM2.5 are also more and more strict. The development of high-performance dust remover is of great significance. In this paper, based on the actual situation of electric bag filter structure optimization, through the classical fluid mechanics software FLUENT6.0 on hydrodynamics conservation equations were established, respectively using UDS and k- programming model of the electric field electric bag filter field establishment and turbulence are described, the numerical simulation of the distribution of pressure drop and electric bag bag electrostatic precipitator zone air distribution and charged particle trajectories and the plate hole in the type area. In the numerical simulation on the basis of trust, different factors (electric field distribution, plate hole, bag distribution) of electric bag filter structure optimization, the minimum particle size, the removal of dust collecting plate geometry factor, the best distribution mode and combined with the bag, the changes of flow parameters on pressure change mechanism analysis. The following conclusions are drawn: (1) the intensity of the electric field in the direction of the air flow is less than the intensity of the electric field in the direction of the dust collector, and the center of the discharge line is the strongest. (2) when the power line is charged with 45k V, the static electric field produces a steady electric field, and the electric field will affect the distribution of the flow field. (3) the minimum electrostatic trapping particle size of 1.5 m, obtained for electric bag composite dust remover, in determining the electrostatic voltage, can be determined within the area of minimum trap size, with the increase of particle size by electric field force larger particles more easily captured; (4) the range of dust the hole plate suitable for 0.324m to 1.25m, the study concluded that dust removal under the conditions of minimum size, can determine the dust collecting plate hole range. (5) through the dust collecting plate is the best opening rate is 0.535 of the dust collector, dust collecting plate with no opening rate increasing the dust collecting plate performance is better, there is the best opening rate; (6) through the analysis of the dust collecting plate is the optimum pore size is 0.095 of the dust remover, and with dust surface roughness increases, the wear plate also increases; the dust collecting plate the best porosity and the pore size and the dust collecting plate wear, facilitates the study for structure design and optimization of dust, which is consistent with the actual structure design. In order to improve the service life of the dust collector, the selection of the roughness of the dust collection board should be carefully considered. (7) the reasonable distribution of filter bag will affect the efficiency of filter bag. In this paper, the electric field, the flow field, the charged particles, the geometric factors of the dust collecting board and the distribution of the filter bags were simulated, and a reference method for the structure optimization of the electric bag filter was provided.
【學(xué)位授予單位】：江西理工大學(xué)
【學(xué)位級(jí)別】：碩士
【學(xué)位授予年份】：2015
【分類號(hào)】：X701.2

【參考文獻(xiàn)】

相關(guān)期刊論文 前7條

1 許秦坤;;一種新型電-袋復(fù)合除塵器的粉塵顆粒運(yùn)動(dòng)規(guī)律分析[J];安全與環(huán)境學(xué)報(bào);2009年02期

2 姚偉;韋巍;;電除塵器比電阻軟件測(cè)算研究與應(yīng)用[J];環(huán)境工程學(xué)報(bào);2012年02期

3 李慶;楊振亞;甘罕;肖振雷;王巧艷;;靜電除塵器煙道進(jìn)口處流場(chǎng)的數(shù)值模擬[J];環(huán)境污染與防治;2012年01期

4 邵波;;淺析如何提高電袋除塵器的運(yùn)行可靠性[J];科學(xué)之友;2012年17期

5 李文勇;王少權(quán);張永;方培根;;循環(huán)半干法脫硫中電袋除塵器改造的分析應(yīng)用[J];有色冶金設(shè)計(jì)與研究;2012年02期

6 龍正偉;宋薔;李水清;姚強(qiáng);;復(fù)合式電袋除塵器的伏安特性[J];中國(guó)電機(jī)工程學(xué)報(bào);2010年14期

7 涂揚(yáng)賡;宋薔;涂功銘;姚強(qiáng);;孔板對(duì)復(fù)合電袋除塵器靜電區(qū)除塵性能影響的實(shí)驗(yàn)研究[J];中國(guó)電機(jī)工程學(xué)報(bào);2013年17期

相關(guān)會(huì)議論文 前1條

1 王民玉;葛清樓;葛慶偉;;電、袋除塵器在燃煤鍋爐煙氣粉塵治理中的應(yīng)用[A];中國(guó)硅酸鹽學(xué)會(huì)環(huán)保學(xué)術(shù)年會(huì)論文集[C];2009年

相關(guān)碩士學(xué)位論文 前2條

1 彭增偉;高壓靜電除塵器電暈放電特性研究[D];河北大學(xué);2005年

2 張靜;電—袋復(fù)合除塵器中氣流分布的數(shù)值模擬[D];華北電力大學(xué)（河北）;2010年

，

本文編號(hào)：1347198