袋式除尘器反吹风清灰效果实验研究

通过实验对袋式除尘器反吹风清灰效果进行了研究.实验表明,清洁滤袋阻力与粉尘层阻力相比可忽略不计,滤袋阻力与过滤风速成正比;反吹风清灰时,滤袋上粉尘负荷越大,清灰效果越好;粉尘剥离率随反吹风风速的增加而提高,当反吹风风速增加到3.5m/min时,剥离率增加趋于平缓.实验结果为袋式除尘器清灰时反吹风风速的选择提供了参考数据.     

基于多组并联控制的高层建筑遇险循环链梯研究

为了解决居住在高层建筑中的人们遇险后安全疏散的问题,研究出一种新颖的无动力链梯逃逸系统。在没有电力资源的情况下,既要解决循环链梯缓降速度,实现平滑控制的问题,又要解决系统长期处于闲置状态,而不影响其可靠性的问题。提出了循环链梯缓降速度多组并联控制的方案;采用液压式并联控制机构,很好地解决了链梯缓降速度的平滑控制及其可靠性的问题;并成功地研制出循环链梯的试验装置,经实际的性能测试表明,具有启动负荷小、运行平稳、工作可靠的特点。     

大型游艺机——过山车的安全性分析

研究基于虚拟样机技术的过山车的安全性问题,旨在解决传统设计的弊端,有效降低设计成本,提高过山车的安全性能。在ADAMS软件中建立过山车的虚拟样机模型。研究轨道圆环直径、车厢重量、制动力对过山车安全性能的影响,获得以上各参数的合理范围,使车厢连接副受力状况与加速度得到改善,制动力精确性得到提高。为探索运动类特种设备———过山车的安全保障技术提供了新途径。     

喷雾降尘效率及喷雾参数匹配研究

采用压力型雾化喷嘴沉降煤矿粉尘简单实用。为了更好地利用喷雾技术高效沉降作业场所的粉尘,采用理论分析的方法得到水雾粒度与水压力之间的关系曲线,进一步得到喷雾降尘效率与水压力之间的关系曲线,并在煤矿井下进行试验验证。从而得出高效沉降粉尘应该用小口径喷嘴和较高的喷雾压力,但应限制在10MPa以下,超过该限值,降尘率提高甚微。2MPa以下的喷雾压力,降尘效率超不过50%,对水资源是一种浪费。当限定喷雾系统的水量消耗时,应采取减小喷嘴口径或减少喷嘴数量的方法获得较高的喷雾压力,从而获得较高的降尘效率。     

涟钢烧结厂成品仓除尘系统的改造

涟钢烧结厂成品仓扩建,老除尘器处理能力有限,无法达到除尘效果,必须改造.长袋低压脉冲袋式除尘器具有清灰能力强,喷吹压力低,过滤风速大,运行能耗低,换袋方便,维修简单等特点,运用于此除尘系统中,取得了良好的除尘效果.     

变频恒压供水控制技术在泵站供水系统中的应用

初步讨论变频恒压供水的基本原理及其在泵站中的应用.通过介绍泵站供水工艺系统的组成、自动化及仪表系统的配置、变频恒压供水的控制原理及监控系统的构成等的泵站供水自动化控制工程实例说明变频恒压供水在泵站中的应用.     

空气加热管路压力损失校核计算

针对自行设计的气体爆炸试验装置中的空气加热管路部分进行了压力损失的计算,并进行了实验验证,通过实验验证该管路达到了设计要求.     

液氦罐车碰撞仿真安全性研究

本文采用s0Mworks、ANSyS／Workbench、LS—DYNA等软件对常温裸形的液氨罐车进行了碰撞仿真研究,获得了多种情形下罐车的碰撞性能,为以后展开实车碰撞提供了重要的技术支撑。     

管道内天然气爆炸火焰及压力波传播规律实验研究

天燃气安全不仅仅局限在企业内部,而是面向全社会,关系到社会稳定和市民生命财产安全。随着天然气市场开拓和广泛利用,庞大的管网系统和多样的用气环境给安全工作提出了更高的要求。采用理论分析、实验研究相结合的方法研究了管道内天然气爆炸火焰及压力波的传播规律。应用直径为700mm,长度为93m的管道进行了三次天然气爆炸传播实验。得出爆源点最大压力值并不是整个爆炸过程的最大值;压力波最大压力值在爆源点附近先降低,然后上升到某一峰值之后再逐渐衰减;最大压力值在衰减过程中不是单调衰减,有点起伏;随着天然气浓度的增大,其爆炸平均升压速率反而减小;随着天然气浓度的增大,其爆炸平均升压速率反而在减小;爆源附近火焰传播速度较小,上升到某一峰值后逐渐衰减。     

Experimental investigation of gas explosion in single vessel and connected vessels

Gas explosion in connected vessels usually leads to high pressure and high rate of pressure increase which the vessels and pipes can not tolerate. Severe human casualties and property losses may occur due to the variation characteristics of gas explosion pressure in connected vessels. To determine gas explosion strength, an experimental testing system for methane and air mixture explosion in a single vessel, in a single vessel connected a pipe and in connected vessels has been set up. The experiment apparatus consisted of two spherical vessels of 350 mm and 600 mm in diameter, three connecting pipes of 89 mm in diameter and 6 m in length. First, the results of gas explosion pressure in a single vessel and connected vessels were compared and analyzed. And then the development of gas explosion, its changing characteristics and relevant influencing factors were analyzed. When gas explosion occurs in a single vessel, the maximum explosion pressure and pressure growth rate with ignition at the center of a spherical vessel are higher than those with ignition on the inner-wall of the vessel. In conclusion, besides ignition source on the inner wall, the ignition source at the center of the vessels must be avoided to reduce the damage level. When the gas mixture is ignited in the large vessel, the maximum explosion pressure and explosion pressure rising rate in the small vessel raise. And the maximum explosion pressure and pressure rising rate in connected vessels are higher than those in the single containment vessel. So whenever possible, some isolation techniques, such as fast-acting valves, rotary valves, etc., might be applied to reduce explosion strength in the integrated system. However, when the gas mixture is ignited in the small vessel, the maximum explosion pressures in the large vessel and in the small vessel both decrease. Moreover, the explosion pressure is lower than that in the single vessel. When gas explosion happens in a single vessel connected to a pipe, the maximum explosion pressure occurs at the end of the pipe if the gas mixture is ignited in the spherical vessel. Therefore, installing a pipe into the system can reduce the maximum explosion pressure, but it also causes the explosion pressure growth rate to increase.